U.S. patent number 6,562,266 [Application Number 09/829,024] was granted by the patent office on 2003-05-13 for composite membrane and method for making the same.
This patent grant is currently assigned to Dow Global Technologies Inc.. Invention is credited to William E. Mickols.
United States Patent |
6,562,266 |
Mickols |
May 13, 2003 |
Composite membrane and method for making the same
Abstract
A composite membrane and method for making the same, comprising
a porous support and a polyamide surface. The subject membrane
provides improved flux and/or rejection rates. The subject membrane
is further capable of operating at lower operating pressures. The
subject method includes reacting a polyfunctional amine with a
polyfunctional acyl halide to form a polyamide. The method includes
the step of contacting a complexing agent with the polyfunctional
acyl halide prior substantial reaction between the polyfunctional
acyl halide and a polyfunctional amine. The subject process is
easily adapted to commercial scale manufacturing processes and is
particularly suited for making nanofiltration and reverse osmosis
composite membranes.
Inventors: |
Mickols; William E.
(Chanhassen, MN) |
Assignee: |
Dow Global Technologies Inc.
(Midland, MI)
|
Family
ID: |
24197538 |
Appl.
No.: |
09/829,024 |
Filed: |
April 9, 2001 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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550527 |
Apr 17, 2000 |
6337018 |
Jan 8, 2002 |
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Current U.S.
Class: |
264/41;
210/500.38; 427/245; 264/48; 427/244 |
Current CPC
Class: |
B01D
71/56 (20130101); B01D 69/125 (20130101) |
Current International
Class: |
B01D
69/12 (20060101); B01D 69/00 (20060101); B01D
71/00 (20060101); B01D 71/56 (20060101); B29C
065/00 (); B05D 005/00 () |
Field of
Search: |
;210/500.38,490
;264/41.48,49 ;427/244,245 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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1 950 594 |
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Apr 1970 |
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DE |
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0 474 370 |
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Mar 1992 |
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EP |
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271847-1988 |
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Oct 1988 |
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JP |
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10 235173 |
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Sep 2001 |
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JP |
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Other References
"Composite Membrane and Method for Making the Same", William E.
Mickols, U.S. Ser. No. 09/550,527, filed Apr. 17, 2000. .
PCT International Search Report corresponding to application No.
PCT/US01/11265. .
Corbridge, D.E.C., Studies in Inorganic Chemistry 6, Phosphorus, An
Outline of its Chemistry, Biochemistry and Technology (Third
Edition), Elsevier, "Phosphorus--Carbon Compounds", Chapter 4, pp.
209-212, 1985. .
Derwent Abstract, JP2000015067A, Manufacture of Composite
Semipermeable Membrane for Recovery of Electrode Deposition Paints
and Pure Water for Washing Semiconductor, etc. with available
selected translated excerpts from patent..
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Primary Examiner: Fortuna; Ana
Parent Case Text
This application is a continuation-in-part of prior application
Ser. No. 09/550,527 filed Apr. 17, 2000 which issued on Jan. 8,
2002 as U.S. Pat. No. 6,337,018 and which is incorporated herein in
its entirety and is relied upon for priority. Reference is further
made to co-pending with U.S. Ser. No. 10/005,455 filed Nov. 2, 2001
which is a continuation of U.S. Pat. No. 6,337,018.
Claims
What is claimed is:
1. A method for making a composite membrane comprising
interfacially polymerizing a polyfunctional amine with a
polyfunctional acyl halide upon a surface of a porous support to
form a polyamide layer thereon, the method characterized by the
step of contacting a complexing agent with the polyfunctional acyl
halide prior to the reaction between the polyfunctional acyl halide
and polyfunctional amine, wherein the complexing agent has a
solubility parameter of from about 15 to about 26 J.sup.1/2
cm.sup.-3/2 and has a binding core selected from non-sulfur atoms
selected from Groups IIIA-VIB and Periods 3-6 of the conventional
IUPAC period table.
2. The method of claim 1 wherein the step of contacting the
complexing agent with the polyfunctional acyl halide results in a
polyamide layer having a detectable quantity of the binding core of
the complexing agent retained therein after the membrane has been
operated in reverse osmosis mode using pure water feed at a 24 gfd
flux rate through the membrane with a permeate recovery between
0.5% to 25% at 25.degree. C. for 24 hours.
3. The method of claim 2 wherein the polyamide layer has at least
25 micrograms of the binding core of the complexing agent retained
therein per gram of polyamide.
4. The method of claim 1 wherein the change in total energy
resulting from the interaction of the polyfunctional acyl halide
and complexing agent is between about 3.5 to 20 kcals/mole.
5. The method of claim 4 wherein the complexing agent has a
solubility parameter of from 18 to 23 J.sup.1/2 cm.sup.-3/2 and
wherein the change in total energy resulting from the interaction
of the polyfunctional acyl halide and complexing agent is between
5.0 to 15.0 kcals/mole.
6. The method of claim 1 wherein the complexing agent is
represented by the formula:
where .alpha. is the binding core, L is a chemical linking group,
the same or different, .beta. is solubilizing group, the same or
different and includes from 1 to 12 carbon atoms, x is an integer
from 0 to 1, and y is an integer from 1 to 5.
7. The method of claim 1 wherein the binding core of the complexing
agent is a metal.
8. The method of claim 1 wherein the binding core of the complexing
agent is selected from silicon and selenium.
9. The method of claim 1 wherein the binding core of the complexing
agent is selected from at least one of the following elements: Al,
Si, P, As, Sb, Bi, Se, Te, Fe, Cr, Co, Ni, Cu, and Zn.
10. The method of claim 1 wherein the polyfunctional amine is
provided as an aqueous solution, the polyfunctional acyl halide is
provided as a non-aqueous solution including the complexing agent
wherein the complexing agent is substantially soluble in said
non-aqueous solution and has a solubility parameter of from about
15 to about 26 J.sup.1/2 cm.sup.-3/2, and wherein the solutions are
sequentially coated upon a surface of the porous support.
11. The method of claim 1 wherein the complexing agent has a
binding core of phosphorous and wherein the complexing agent is
selected from at least on of the following classes of compounds:
phosphates, phosphites, phosphines, phosphine oxides, phosphonates,
diphosphonates, phosphinates, phosphinites, phosphonites,
pyrophosphates, pyrophosphoramides, phosphor amides,
phosphorothionates, phosphorodithionates, and phosphoroamido
thionates.
12. The method of claim 1 wherein the complexing agent comprises a
compound represented by the formula: ##STR5##
wherein Z is the same or different and is selected from: X,
O--P--(X).sub.2, P(O)--X.sub.2, (P(--X)).sub.m --P--X.sub.2,
(O--P(--X)).sub.m --O--P--X.sub.2, (P(O)(--X)).sub.m
--P(O)--X.sub.2, and (O--P(O)--X)).sub.m --O--P(O)--X.sub.2 ; P is
phosphorous, O is oxygen, m is an integer from 1 to 5; Y is O or a
non-bonded pair of electrons, X is the same or different and is
selected from: R and R including one or more oxygen and/or alkyl
linkage(s), and R is the same or different and is selected from H,
and a carbon containing moiety.
13. The method of claim 12 wherein Z is selected from C.sub.1
-C.sub.8 aliphatic groups.
14. The method of claim 12 wherein at least one R is selected from
an aromatic group or heterocyclic group.
15. The method of claim 12 wherein Y is oxygen; Z is the same or
different and is selected from R and R including one or more oxygen
linkages; and R is the same or different and is selected from: H
and C.sub.1 -C.sub.12 containing moiety.
16. The method of claim 15 wherein R is selected from C.sub.1
-C.sub.8 aliphatic groups.
17. The method of claim 15 wherein at least one R is selected from
an aromatic group and/or heterocyclic group.
18. The method of claim 15 wherein the phosphorous containing
compound comprises a compound represented by the formula:
##STR6##
19. The method of claim 18 wherein R is selected from C.sub.1
-C.sub.8 aliphatic groups.
20. The method of claim 18 wherein at least one R is selected from
an aromatic and/or heterocyclic group.
21. The method of claim 12 wherein Y is a non-bonded pair of
electrons and the phosphorous containing compound comprises a
compound represented by the formula: ##STR7##
wherein Z is the same or different and is selected from R and R
including one or more oxygen and/or alkyl linkages; and R is the
same or different and is selected from: H and C.sub.1 -C.sub.12
containing moiety.
22. The method of claim 21 wherein R is selected from C.sub.1
-C.sub.8 aliphatic groups.
23. The method of claim 21 wherein at least one R is selected from
an aromatic group.
24. The method of claim 21 wherein at least one R is selected from
an heterocyclic group.
25. A method for making a composite membrane comprising the steps
of coating a porous support with an aqueous solution containing a
polyfunctional amine followed by subsequently coating an organic
solution containing a polyfunctional acyl halide such that the
polyfunctional amine and polyfunctional acyl halide are contacted
with each other and react to form a polyamide layer on the porous
support, the method characterized by the step of contacting a
complexing agent with the polyfunctional acyl halide prior to the
reaction between the polyfunctional acyl halide and polyfunctional
amine, wherein the complexing agent has a solubility parameter of
from about 15 to about 26 J.sup.1/2 cm.sup.-3/2 and has a binding
core including at least one atom selected from non-sulfur elements
selected from Groups IIIA-VIB and Periods 3-6 of the conventional
IUPAC period table.
26. The method of claim 25 wherein the binding core of the
complexing agent is selected from at least one of the following
elements: Al, Si, P, As, Sb, Se, Te, Fe, Cr, Co, Ni, Cu, Zn and Pb.
Description
BACKGROUND OF THE INVENTION
Reverse osmosis and nanofiltration membranes are used to separate
dissolved or dispersed materials from feed streams. The separation
process typically involves bringing an aqueous feed solution into
contact with one surface of the membrane under pressure so as to
effect permeation of the aqueous phase through the membrane while
permeation of the dissolved or dispersed materials is
prevented.
Both reverse osmosis and nanofiltration membranes typically include
a thin film discriminating layer fixed to a porous support,
collectively referred to as a "composite membrane". Ultrafiltration
and microfiltration membranes may also have a composite
arrangement. The support provides physical strength but offers
little resistance to flow due to its porosity. On the other hand,
the discriminating layer is less porous and provides the primary
means of separation of dissolved or dispersed materials. Therefore,
it is generally the discriminating layer which determines a given
membrane's "rejection rate"--the percentage of the particular
dissolved material (i.e., solute) rejected, and "flux"--the flow
rate per unit area at which the solvent passes through the
membrane.
Reverse osmosis membranes and nanofiltration membranes vary from
each other with respect to their degree of permeability to
different ions and organic compounds. Reverse osmosis membranes are
relatively impermeable to virtually all ions, including sodium and
chlorine ions. Therefore, reverse osmosis membranes are widely used
for the desalination of brackish water or seawater to provide
relatively non-salty water for industrial, commercial, or domestic
use because the rejection rate of sodium and chlorine ions for
reverse osmosis membranes is usually from about 95 to about 100
percent.
Nanofiltration membranes are usually more specific for the
rejection of ions. Generally, nanofiltration membranes reject
divalent ions, including radium, magnesium, calcium, sulfate, and
carbonate. In addition, nanofiltration membranes are generally
impermeable to organic compounds having molecular weights above
about 200 Daltons. Additionally, nanofiltration membranes generally
have higher fluxes at comparable pressures than reverse osmosis
membranes. These characteristics render nanofiltration membranes
useful in such diverse applications as the "softening" of water and
the removal of pesticides from water. As an example, nanofiltration
membranes generally have a sodium chloride rejection rate of from
about 0 to about 95 percent but have a relatively high rejection
rate for salts such as magnesium sulfate and in some cases organic
compounds such as atrazine.
Among particularly useful membranes for reverse osmosis and
nanofiltration applications are those in which the discriminating
layer is a polyamide. The polyamide discriminating layer for
reverse osmosis membranes is often obtained by an interfacial
polycondensation reaction between a polyfunctional amine monomer
and a polyfunctional acyl halide monomer (also referred to as
polyfuntional acid halide) as described in, for example, U.S. Pat.
No. 4,277,344, which is incorporated herein by reference. The
polyamide discriminating layer for nanofiltration membranes is
typically obtained via an interfacial polymerization between a
piperazine or an amine substituted piperidine or cyclohexane and a
polyfunctional acyl halide as described in U.S. Pat. Nos. 4,769,148
and 4,859,384, both incorporated in their entirety by reference.
Another way of obtaining polyamide discriminating layers suitable
for nanofiltration is via the methods described in, for example,
U.S. Pat. Nos. 4,765,897; 4,812,270; and 4,824,574. These patents
describe changing a reverse osmosis membrane, such as those of U.S.
Pat. No. 4,277,344, into a nanofiltration membrane.
Composite polyamide membranes are typically prepared by coating a
porous support with a polyfunctional amine monomer, most commonly
coated from an aqueous solution. Although water is a preferred
solvent, non-aqueous solvents may be utilized, such as acetyl
nitrile and dimethylformamide (DMF). A polyfunctional acyl halide
monomer (also referred to as acid halide) is subsequently coated on
the support, typically from an organic solution. Although no
specific order of addition is necessarily required, the amine
solution is typically coated first on the porous support followed
by the acyl halide solution. Although one or both of the
polyfunctional amine and acyl halide may be applied to the porous
support from a solution, they may alternatively be applied by other
means such as by vapor deposition, or neat.
Means for improving the performance of membranes by the addition of
constituents to the amine and/or acyl halide solutions are
described in the literature. For example, U.S. Pat. No. 4,950,404,
issued to Chau, describes a method for increasing flux of a
composite membrane by adding a polar aprotic solvent and an
optional acid acceptor to the aqueous amine solution prior to
interfacially polymerizing the amine with an polycarboxylic acid
halide. Similarly, U.S. Pat. Nos. 6,024,873; 5,989,426; 5,843,351;
5,733,602; 5,614,099; and 5,576,057 to Hirose et al. describes the
addition of selected alcohols, ethers, ketones, esters, halogenated
hydrocarbons, nitrogen-containing compounds and sulfur-containing
compounds having a solubility parameter of 8 to 14
(cal/cm.sup.3).sup.1/2 to the aqueous amine solution and/or organic
acid halide solution prior to interfacial polymerization.
Methods of improving membrane performance by post-treatment are
also known. For example, U.S. Pat. No. 5,876,602 to Jons et al.
describes treating a polyamide composite membrane with an aqueous
chlorinating agent to improve flux, lower salt passage, and/or
increase membrane stability to base. U.S. Pat. No. 5,755,964 to
Mickols discloses a process wherein the polyamide discriminating
layer is treated with ammonia or selected amines, e.g., butylamine,
cyclohexylamine, and 1,6 hexane diamine. U.S. Pat. No. 4,765,897 to
Cadotte discloses the post treatment of a membrane with a strong
mineral acid followed by treatment with a rejection enhancing
agent. U.S. Pat. Nos. 4,765,897; 5,876,602 and 5,755,964 are
incorporated herein by reference.
Membranes having higher flux at standard operating pressures, or
which are capable of maintaining flux at relatively lower operating
pressures are desired. Moreover, membranes having higher rejection
rates while achieving improved flux and/or lower pressure
requirements are also desired. Methods for making such membranes,
particularly those readily adaptable to commercial scale membrane
fabrication are also desired.
SUMMARY OF THE INVENTION
The present invention provides an improved composite membrane and
method for making the same by interfacially polymerizing a
polyfunctional amine and a polyfunctional acyl halide on at least
one surface of a porous support to form a polyamide layer thereon.
The method is characterized by the step of contacting a complexing
agent with the polyfunctional acyl halide prior to and/or during
the reaction between the polyfunctional acyl halide and
polyfunctional amine.
An object of the present invention is to provide improved membranes
having higher flux and/or more preferred rejection characteristics
(i.e. higher or lower depending upon the intended end use of the
membrane). A further object of the present invention is to provide
membranes capable of operating at relatively lower pressures while
still providing a given flux and/or rejection. Still another object
of the present invention is to provide methods for making such
membranes, including methods which are readily adaptable to
commercial scale membrane manufacturing. The subject method is
particularly suited for making nanofiltration and reverse osmosis
membranes.
DETAILED DESCRIPTION OF THE INVENTION
Composite membranes of the present invention are prepared by
interfacially polymerizing a polyfunctional amine monomer (also
referred to herein as "amine", "polyamine", and "polyfunctional
amine"--wherein each term is intended to refer both to the use of a
single species or multiple species of amines in combination) with a
polyfunctional acyl halide (also referred to as "acyl halide",
"acid halide", polyfunctional acid halide--wherein each term is
intended to refer both to the use of a single species or multiple
species of acyl halides in combination) on at least one surface of
a porous support. The amine and acyl halide are typically delivered
to the porous support by way of a coating step from solution
wherein the amine is typically coated from an aqueous solution and
the acyl halide is coated from a non-aqueous, organic-based
solution. Although the coating steps can be "non-sequential" i.e.
follow no specific order, the amine is preferably coated on the
support first followed by the acyl halide. Coating may be
accomplished by spraying, rolling, use of a dip tank, etc. Excess
solution may be removed from the support by air and/or water knife,
dryers, ovens, etc.
The polyfunctional amine monomer used in the present invention may
have primary or secondary amino groups and may be aromatic (e.g.,
m-phenylenediamine, p-phenyenediamine, 1,3,5-triaminobenzene,
1,3,4-triaminobenzene, 3,5-diaminobenzoic acid, 2,4-diaminotoluene,
2,4-diaminoanisole, and xylylenediamine) or aliphatic (e.g.,
ethylenediamine, propylenediamine, and tris(2-diaminoethyl)amine).
Examples of preferred amine species include primary aromatic amines
having two or three amino groups, most especially m-phenylene
diamine, and secondary aliphatic amines having two amino groups,
most especially piperazine. The amine is typically applied to the
microporous support as a solution in water. The aqueous solution
most commonly contains from about 0.1 to about 20 weight percent
and more preferably from about 0.5 to about 6 weight percent amine.
Once coated on the microporous support, excess aqueous amine
solution may be optionally removed. The amine solution need not be
aqueous but is preferably immicible with the non-polar non-aqueous
solvent described below.
As previously indicated, the monomeric polyfunctional acyl halide
is preferably coated from a non-polar solvent, although the
polyfunctional acyl halide may be delivered from a vapor phase (for
polyfunctional acyl halides having sufficient vapor pressure). The
polyfunctional acyl halides are preferably aromatic in nature and
contain at least two and preferably three acyl halide groups per
molecule. Because of their lower cost and greater availability,
chlorides are generally preferred over the corresponding bromides
or iodides. One preferred polyfunctional acyl halide is trimesoyl
chloride (TMC). The polyfunctional acyl halide is typically
dissolved in a non-polar organic solvent in a range of from 0.01 to
10.0 weight percent (more preferably 0.05 to 3 weight percent), and
delivered as part of a continuous coating operation. Suitable
non-polar solvents are those which are capable of dissolving
polyfunctional acyl halides and which are immiscible with water.
Preferred solvents include those which do not pose a threat to the
ozone layer and yet are sufficiently safe in terms of their
flashpoints and flammability to undergo routine processing without
having to undertake extreme precautions. Higher boiling
hydrocarbons, i.e., those with boiling points greater than about
90.degree. C. such as C.sub.8 -C.sub.14 hydrocarbons and mixtures
thereof have more favorable flashpoints than their C.sub.5 -C.sub.7
counterparts but they are less volatile.
Once brought into contact with one another, the polyfunctional acyl
halide and polyfunctional amine react at their surface interface to
form a polyamide discriminating layer. The reaction time is
typically less than one second but contact time is often from one
to sixty seconds, after which excess liquid may optionally be
removed, e.g., by way of an air knife, water bath(s), dryer and the
like. The removal of the excess water and/or organic solvent is
most conveniently achieved by drying at elevated temperatures,
e.g., from about 40.degree. C. to about 120.degree. C., although
air drying at ambient temperatures may be used.
While not wishing to be bound by theory, it is believed that the
acyl halide functional groups of the polyfunctional acyl halide
monomer often become hydrolyzed prior to contact with amine
functional groups. Under typical manufacturing conditions, such
hydrolysis of acyl halide functional groups is substantially
irreversible. That is, under the time, temperature and
concentrations typically used in commercial scale membrane
manufacturing, amine functional groups are not believed to
substantially react with hydrolyzed acyl halide groups. It is
believed that such hydrolysis of acyl halide groups leads to
compromised membrane performance.
While not wishing to be bound by theory, it is believed that the
subject complexing agents are capable of forming "associations"
with the polyfunctional acyl halide monomers when utilized in
accordance with the subject method. It is believed that the
formation of such associations significantly reduce hydrolysis of
the acyl halide functional groups and permits sufficient subsequent
reaction between the acyl halide and amine functional groups
thereby resulting in the aforementioned improvements in membrane
performance.
The term "associations" is intended to describe the chemical
interaction formed between the subject complexing agents and the
polyfunctional acyl halide prior to or during the reaction of the
amine and acyl halide functional groups. Such associations can also
be described in terms of the elimination of repulsive forces
between the polyfunctional acyl halide and other components of a
solution.
Another way to describe the interaction between the acyl halide and
complexing agent is in terms of the "change in total energy"
resulting from their combination. In layman's terms, this is the
change in energy resulting from the formation of associations
between the complexing agent and acyl halide. In more formal terms,
total energy "U" can be defined per Equation I: ##EQU1##
see for example H. Callan's "Thermodynamics", (John Wily & Son,
New York, 1960). The change (.DELTA.) in total energy ".DELTA.U"
resulting from the combination of distinct chemical species can be
represented by Equation II: ##EQU2##
where u is the chemical potential of each chemical species (e.g.
TMC and the complexing agent), N is the number of moles of each
chemical species, T is the Temperature, S is the entropy, P is the
pressure, V is the volume of the system, i and m are integers
starting with "one" where m represents the total number of chemical
species within the system. The total energy is closely related to
several other representations of energy that have experimental
limitations. For example, free energy ".mu." is commonly used for
reactions that occur at atmospheric pressure and can be represented
by Equation III:
where n equals the number of moles of the associated species (e.g.
reaction product of the acyl halide monomer and complexing agent),
G is the Gibbs free energy, T is the Temperature, S is the entropy,
P is the pressure and V is the volume of the system. G can be
defined according to Equation IV:
where H is the enthalpy of the system. All references to energy and
related terms and symbols are intended to be consistent with
standard chemical convention.
When combined with acyl halide, the complexing agents of the
subject invention preferably result in a change in total energy
(.DELTA.U) from about 3.5 to 20 kcals/mole, and more preferably
from about 5 to 15 kcals/mole, and still more preferably of from 5
to 10 kcals/mole. Within the context of the present invention, the
change in total energy resulting from the combination of the acyl
halide and the complexing agent is approximately equal to the
change in Gibbs free energy and enthalpy, i.e.
U.apprxeq.G.apprxeq.H. Thus, one skilled in the art can typically
determine the suitability of a given complexing agent for use with
a particular acyl halide species by measuring the enthalpy (H)
generated from their combination. Calorimetric methods for
determining enthalpy of a system are well known.
For many embodiments, the total energy and/or enthalpy of the
interaction of a given complexing agent and acyl halide is
approximately equal to the total energy and/or enthalpy of the
system used under manufacturing conditions. That is, the change in
total energy or enthalpy of interaction between the acyl halide and
complexing agent can be approximated by measuring the change in
enthalpy of the system to which the complexing agent is added, e.g.
the acyl halide coating solution including the acyl halide,
solvent, additives, impurities, etc. For embodiments wherein the
complexing agent is contacted with the acyl halide from the amine
solution, the applicable "system" may be further complicated by
additional chemical species, e.g. amine, water, etc. In the final
analysis, it is the change in total energy resulting from the
interaction between the acyl halide and complexing agent that is
most relevant. With that said, it should be appreciated that the
reaction medium can have a significant impact on the change in
total free energy of the system. For example, in preferred
embodiments the acyl halide and complexing agent are both
substantially soluble in the solution from which they are
coated.
Associations which are too weak (i.e. have a total energy value
less about 3.5 kcals/mole) result in associations that do not
effectively prevent hydrolysis of the acyl halide functional
groups. As will be described below, one measure of a sufficiently
strong association is the presence of a "detectable quantity" of
"retained" complexing agent within the polyamide, even after post
washing of the membrane. On the other hand, associations which are
too strong (i.e. have a total energy of more than about 20 or
preferably 15 kcals/mole) do not permit sufficient displacement and
reaction by amines during membrane formation, thus preventing the
formation of the desired polyamide. An example of an association
which is too strong is the hydrolysis of an acid chloride group of
TMC under common manufacturing conditions which results in a total
energy value of greater than about 25 kcals/mole.
In order to provide the full benefit of the subject invention, it
is believed that it is important to form the described association
between the complexing agent and the acyl halide prior to or during
the reaction between the acyl halide and amine. Thus, the timing
and manner of addition of the complexing agent are believed to be
important. For example, the benefit of the subject invention is not
achieved by the sole addition of a phosphoric acid (e.g., as
described in U.S. Pat. No. 4,765,897) after the acyl halide and
amine have substantially reacted. Moreover, the benefit of the
invention is not achieved if the complexing agent is contacted with
the acyl halide in a manner which does not permit the formation of
an association therebetween. For example, if a particular
complexing agent is insufficiently soluble or dispersible within an
acyl halide solution, it is unlikely that the full benefits of the
subject invention will be realized as an insufficient degree of
association will occur. Consequently, preferred embodiments of the
invention utilize complexing agents which are substantially soluble
in the acyl halide solution and which readily form associations
with acyl halides. As described elsewhere, preferred complexing
agents have a solubility parameter of from about 15 to about 26,
and more preferably from 18 to 23 J.sup.1/2 cm.sup.-3/2.
In preferred embodiments, the subject complexing agent is directly
added to the acyl halide solution prior to contacting (e.g.
coating) the acyl halide and amine solutions, thereby permitting
sufficient opportunity for the formation of an association prior to
reaction between the amine and acyl halide. Alternatively, the acyl
halide and complexing agent may be contacted "neat" and
subsequently added to solution for coating.
In a less preferred alternative embodiment, the complexing agent(s)
may be contacted with the acyl halide solution (e.g., via spray)
while the acyl halide solution is contacted with the polyfunctional
amine solution. In this embodiment, the complexing agent is
essentially contacted with the acyl halide solution simultaneously
with the step of contacting the acyl halide and amine solution but
prior to complete reaction between the amine and acyl halide. In
this embodiment the acyl halide and complexing agent have a much
shorter time period to form a complex prior to complete reaction
between the acyl halide and amine. Alternatively, the complexing
agent may be contacted with the acyl halide solution after the acyl
halide and amine solutions have been contacted but prior to
complete reaction therebetween. As previously indicated, this
embodiment provides a much shorter time period for complex
formation to occur prior to complete reaction between the acyl
halide and amine.
In a still less preferred embodiment, the complexing agent may be
coated on the support or added to the amine solution prior to
contacting the amine and acyl halide solutions. These approaches
are less preferred as it is difficult to deliver the complexing
agent to the acyl halide in a manner which allows suitable complex
formation prior to completion of the reaction between the acyl
halide and amine. However, one remedial approach includes the
formation of a high internal phase emulsion of the complexing agent
within the amine solution, thereby providing a relatively uniform
delivery of the complexing agent to the acyl halide during reaction
between the acyl halide and amine. Formation of high internal phase
emulsions are well known and are described in U.S. Pat. No.
5,977,194 which is incorporated herein by reference. Other suitable
approaches involve the selection of complexing agents having
sufficient solubility in the amine solution (e.g., aqueous
solutions) in order to be uniformly dispersed, while simultaneously
being sufficiently soluble in the acyl halide solution (e.g.,
organic solution) such that a sufficient amount of complexing agent
is provided to the acyl halide prior to completion of reaction
between the acyl halide and amine.
The embodiments described above may be used in combination, e.g.
the subject complexing agent may be added to both the acyl halide
and amine solutions prior to contacting the solutions.
Alternatively, the complexing agent may be added to either solution
while also being applied via spray or vapor deposition during the
step of coating the solutions.
One means for determining whether the subject complexing agent(s)
have been successfully contacted with the acyl halide in accordance
to the subject method is the presence of a "detectable quantity" of
"retained" complexing agent in the polyamide membrane. The term
"retained" is intended to mean complexing agent which remains
(e.g., associated, covalently bonded, complexed, weakly bound,
etc.) within the polyamide membrane even after the membrane has
been subjected to operation in reverse osmosis mode using pure
water feed at a 24 gfd (gallons per square foot per day) (0.0011
cm/sec) flux rate through the membrane with a permeate recovery
between 0.5% to 25% at 25.degree. C. for 24 hours. This may be
accomplished by use of test cells commonly used to test membranes.
For example, the test cell may be of a "plate and frame" design or
may include preparing a spiral wound element with the membrane.
Cleaning with pure water, e.g. passing pure water across the
polyamide membrane at 25.degree. C. for 24 hours at a pressure of
about 70 pounds per square inch. Such cleaning removes transient
sources of materials which may be initially present but which do
not contribute to the subject invention. For example, it is well
known that phosphoric acid may be added to the amine solution as a
pH buffer. In such embodiments some portion of the phosphoric acid
may be present on the initial resulting membrane; however, as the
phosphoric acid is not contacted with the acyl halide in manner
which permits sufficient association, the phosphoric acid is not
retained and is washed away from the membrane upon use or cleaning.
Although such prior art uses of phosphoric acid may be used in
conjunction with the subject invention, such prior art embodiments
do not result in "retained" phosphorous, nor the degree of improved
membrane performance attributed to the subject invention.
The term "detectable quantity" is intended to mean a sufficient
quantity of retained complexing agent is present such that it may
be measured, identified or otherwise detected by quantitative or
qualitative analysis. Detection of such complexing agents in
membranes can be made by way of any suitable analytical technique;
however due to the relatively low quantities of complexing agent
typically utilized, relatively sensitive analytical techniques are
preferred, e.g. gas chromatography, X-ray fluorescence, (XRF),
secondary ion mass spectroscopy, IR, and colorimetric analysis of
the fully combusted polyamide. Detection of the complexing agent
typically focuses upon the binding core of the complexing agent. As
described in more detail below, the binding core often comprises
metals, e.g. Pb, Fe, Cr, Ni, Co, Cu, Zn, Al, As, Sb, Te, etc. but
may include other elements, e.g. P, Si, Se, Ge, etc. One specific
X-ray fluorescence detection methodology is particularly well
suited for detecting phosphorous containing complexing agents and
involves extracting a portion (e.g., 100 mg) of the polyamide
polymer from the porous support, e.g., boiling the membrane in
water for about 30 minutes followed by dissolving the porous
support with an appropriate solvent, e.g., methylene chloride, and
subsequently extensively extracting the polyamide in the same
solvent. The polyamide may then be isolated and pressed into a 13
mm diameter disk using a die and an hydraulic press (10,000 lbs.
load). The resulting disk may be placed between two layers of
polypropylene sample support film (6.0 micron thickness) and
attached to a Chemplex 30 mm diameter XRF sample cup using a
standard support ring. The sample can be measured in a plastic
insert with a Pb mask. Measurements can be obtained on both sides
of the disk and averaged together. Once prepared, the sample can be
analyzed with a Philips PW1480 wavelength dispersive X-ray
fluorescence spectrometer equipped with a scandium anode 3KW X-ray
tube. For example, phosphorous can be measured by utilizing K alpha
X-ray intensity with the instrument operated under the following
conditions: 50 kV, 50 mA, germanium crystal (2d=6.532 angstroms),
gas flow proportional detector (argon/methane), upper and lower
discriminator level 80/25, He purge. The phosphorous K alpha peak
can be measured at a 2 theta angle of 141.035 and backgrounds can
be measured at + and - offsets of 1.5. Peak and background
measurements are commonly taken for 10 seconds each.
In preferred embodiments, the subject polyamide composite membrane
includes at least about 25 micrograms (and preferably at least 50
micrograms, more preferably 100 micrograms and in some embodiments
at least 200 micrograms) of the binding core of the complexing
agent "retained" for every gram of polyamide. The elements that
constitute the binding core of the subject complexing agents are
not typically present during conventional membrane preparation. As
such, these elements serve as a good indicator as to whether the
subject complexing agents have been used effectively during
membrane preparation.
As indicated, the retained complexing agent is believed to be a
result of the formation of a complex between the complexing agent
and the polyamide, retained monomers, and/or reaction products.
Although dependent upon the relative density of the polyamide
layer, most membranes of the subject invention will include at
least 0.02 micrograms of complexing agent per square meter of
membrane, but more commonly more than about 1 microgram of
complexing agent per square meter of membrane.
The complexing agents of the present invention are not particularly
limited and different species of compounds may be used in
combination. However, preferred species are non-pyrophoric,
sufficiently stable in air and water (i.e., the species do not
decompose, degrade or significantly react with water or air within
the time period of the subject method), and have suitable
industrial hygiene properties, e.g., do not pose significant
environmental hazards, do not require expansive handling
requirements, do not pose significant safety concerns, etc. The
subject complexing agents are preferably "substantially soluble" in
the organic solutions as described herein. The term "substantially
soluble" is intended to mean that a sufficient quantity of the
complexing agent dissolves in the solution to result in a final
membrane having improved flux, rejection and/or lower operating
pressure as compared to an identical membrane prepared without the
subject complexing agent. An additional indicia that the complexing
agent is "substantially soluble" is the presence of a detectable
quantity of retained complexing agent in the polyamide layer. When
used at effective concentrations the subject complexing agents
preferably dissolve and form a single homogeneous phase within the
organic solutions previously described. Preferred complexing agents
have a solubility parameter of from about 15 to about 26, and more
preferably from 18 to 23 J.sup.1/2 cm.sup.-3/2.
Regardless of the means of contacting the complexing agent with the
acyl halide solution, the quantity of complexing agent is
preferably stoichiometrically related to the quantity of
polyfunctional acyl halide. Preferred stoichiometric ratios of
complexing agent to polyfunctional acyl halide range from about 1:5
to about 5:1 with 1:1 to about 3:1 being most preferred. Although
preferred, stoichiometric ratios of the complexing agent are not
required. When combined directly with the acyl halide solutions,
the complexing agent typically comprises from about 0.001 to about
2 weight percent of the acyl halide solution. When utilized
according to alternative embodiments as previously described,
larger quantities of the complexing agent may be required.
Unlike conventional interfacial polymerization of polyfunctional
acyl halide and polyfunctional amines in which the relative
concentration of the acyl halide species is rate controlling, in
the present invention the relative concentration of the amine
species may take on a more significant role. Through routine
experimentation, those skilled in the art will appreciate the
optimum concentration of polyfunctional amine, given the specific
nature and concentration of the complexing agent(s), acyl halide,
and amine, reaction conditions and desired membrane
performance.
The subject complexing agents include a wide variety of compounds
which may be generally described according to Formula I:
where .alpha. is a non-sulfur containing binding core selected from
elements falling within: (a) Group IIIA-VIB (i.e. Groups IIIA, IVA,
VA, VIA, VIIA, VIIIA, IB, IIB, IIIB, IVB, VB, VIB) and (b) Periods
3-6 (i.e. Periods starting with Na, K, Rb, and Cs) of the
conventional IUPAC periodic table. Groups IIIA through VIB of the
conventional IUPAC form of the Periodic Table corresponds to:
Groups 3-16 of the "new notation" IUPAC Periodic Table and Groups
IIIB-VIA of the CAS version of the Periodic Table. In order to
avoid any confusion further reference herein will utilize the
conventional IUPAC Periodic Table, i.e. Group IIIA corresponds to
the column starting with Sc, Y, La, etc, and Group VIB corresponds
to the column starting with O, S, Se, Te, Po. Specific examples
include: (1) the following metals: aluminum, scandium, titanium,
vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc,
gallium, germanium, arsenic, yttrium, zirconium, niobium,
molybdenum, technetium, ruthenium, rhodium, palladium, silver,
cadmium, indium, tin, antimony, tellurium, lanthanum, cerium,
praseodymium, neodymium, promethium, samarium, europium,
gadolinium, terbium, dysprosium, holmium, erbium, thulium,
ytterbium, lutetium, hafnium, tantalum, tungsten, rhenium, osmium,
iridium, platinum, gold, mercury, thallium, lead, bismuth (bismuth
is not typically preferred), and polonium; (2) the following
semi-conductors: silicon, selenium, and germanium and (3)
phosphorous. Particularly preferred binding cores include: Al, Si,
P, As, Sb, Se and Te and metals such as: Fe, Cr, Co, Ni, Cu, and
Zn. L is an optional chemical linking group, the same or different,
selected from linkages such as: carbon containing moieties, e.g.
aromatic groups, alkanes, alkenes, --O--, --S--, --N--, --H--,
--P--, --O--P--, and --O--P--O--, (each of which may be substituted
or unsubstituted). .beta. is solubilizing group, the same or
different, and includes from 1 to 12 carbon atoms which may be
substituted or unsubstituted and which may include internal linking
groups as defined by L. Examples include aliphatic and arene groups
having 1 to 6 carbon atoms, aromatic groups, heterocyclic groups,
and alkyl groups. "x" is an integer from 0 to 1 and "y" is an
integer from 1 to 5, preferably from 2 to 4.
Although dependant upon the specific solvent(s) and acyl halide
species utilized, the following complexing agents are generally
useful in the subject invention: tri-phenyl derivatives of
phosphorous (e.g. phosphine, phosphate), bismuth, arsenic and
antimony; alkane oxy esters of phosphorous including tributyl and
dibutyl phosphite; organo-metallic complexes such as ferrocene and
tetraethyl lead, and acetylacetonate complexes of iron (II), iron
(III), cobalt (III) and Cr (III).
Complexing agents including a phosphorus binding core have been
found to be particularly preferred. A preferred class of such
phosphorous containing compounds can be represented below by
following Formula 1: ##STR1##
wherein Z is the same or different and is selected from X,
O--P--(X).sub.2, P(O)--X.sub.2, (P(--X)).sub.m --P--X.sub.2,
(O--P(--X)).sub.m --O--P--X.sub.2, (P(O)(--X)).sub.m
--P(O)--X.sub.2, and (O--P(O)(--X)).sub.m --O--P(O)--X.sub.2,
wherein P is phosphorous, O is oxygen, m is an integer from 1 to 5;
and Y is O (oxygen) or a non-bonded pair of electrons, as indicated
in Formula 2 and 3, respectively; ##STR2## ##STR3##
wherein X is the same or different and is selected from: R or R
including oxygen and/or alkyl linkage(s), e.g., R--O--R, O--R, etc;
and R is the same or different and is selected from H (hydrogen),
and/or a carbon containing moiety. The Z groups are preferably
selected such that they collectively result in the phosphorous
containing compound being substantially soluble in the organic
solution.
The phrase "the same or different" is intended to mean that the
individual groups represented by a single symbol, e.g., "R", may
vary within a given compound. For example, for any given compound,
one R group may be hydrogen whereas the other R groups may be butyl
groups.
The term "carbon containing moiety" is intended to mean branched
and unbranched acyclic groups, e.g., methyl, ethyl, propyl,
isopropyl, butyl, isobutyl, pentyl, 2-pentyl, 3-pentyl, tert-butyl,
etc. which may be unsubstituted or substituted (e.g., substituted
with amide groups, ether groups, ester groups, sulfone groups,
carbonyl groups, anhydrides, cyanide, nitrile, isocynate, urethane,
beta-hydroxy ester, double and triple bonds etc.), and cyclic
groups, e.g., cyclo pentyl, cyclo hexyl, aromatics, e.g., phenyl,
heterocyclic (e.g. pryridine), etc., which may be unsubstituted or
substituted, (e.g., substituted with methyl, ethyl, propyl,
hydroxyl, amide, ether, sulfone, carbonyl, ester, etc.). Cyclo
moieties may be linked to the phosphorous atom by way of an
aliphatic linking group, e.g., methyl, ethyl, etc.
Preferred carbon containing moieties include unsubstituted,
branched or unbranched C.sub.1 -C.sub.12 groups, and more
preferably C.sub.1 -C.sub.8 aliphatic groups such as: methyl,
ethyl, propyl, isopropyl, butyl, 2-methyl butyl, 3-methyl butyl,
2-ethyl butyl, pentyl, hexyl, etc. Additionally, preferred moieties
include phenyl groups.
Examples of preferred sub-classes of compounds are represented by
Formulae 4-9. ##STR4##
wherein R, P and O are as previously defined. Such phosphorous
containing compounds are commercially available or can be
synthesized using known methodologies, see for example U.S. Pat.
No. 2,648,696 to Whetstone, incorporated herein by reference, and
Aharoni et al., Journal of Polymer Science, Volume 22,
2579-2599.
The phosphorous nomenclature utilized herein is intended to be
consistent with that used in D. Corbridge's Studies in Inorganic
Chemistry, 6: Phosphorous--An Outline of its Chemistry,
Biochemistry and Technology, third ed., (Elsevier 1985). Examples
of classes of applicable phosphorous containing compounds include:
phosphates (e.g., phosphate esters), phosphites, phosphines,
phosphine oxides, phosphonates, including diphosphonates,
phosphinates, phosphinites, phosphonites, pyrophosphates,
pyrophosphoramides, phosphor amides, phosphorothionates including
phosphoro dithionates, phosphorodithionates, phosphoro amido
thionates, and phosphonothioates including phosphonodithioates. A
non-comprehensive list of specific examples of each class are
provided below.
Specific examples of tri-phosphates include: tri-methyl phosphate,
tri-ethyl phosphate, tri-(1-propyl) phosphate, tri-(2-propyl)
phosphate, tri-(1-butyl) phosphate, tri-(2-butyl) phosphate,
tri-(1-tert-butyl) phosphate, tri-(2-tert-butyl) phosphate,
tri-(1-pentyl) phosphate, tri-(2-pentyl) phosphate, tri-(3-pentyl)
phosphate, tri-(1-hexyl) phosphate, tri-(2-hexyl) phosphate,
tri-(3-hexyl) phosphate, tri-(1-heptyl) phosphate, tri-(2-heptyl)
phosphate, tri-(3-heptyl) phosphate, tri-(4-heptyl) phosphate,
tri-(1-octyl) phosphate, tri-(2-octyl) phosphate, tri-(3-octyl)
phosphate, tri-(4-octyl) phosphate, tri-(1-CH3(CH2)8) phosphate,
tri-(2-CH3(CH2)8) phosphate, tri-(3-CH3(CH2)8) phosphate,
tri-(4-CH3(CH2)8) phosphate, tri-(1-CH3(CH2)9) phosphate,
tri-(2-CH3(CH2)9) phosphate, tri-(3-CH3(CH2)9) phosphate,
tri-(4-CH3(CH2)9) phosphate, tri-(5-CH3(CH2)9) phosphate,
tri-(1-CH3(CH2)10) phosphate, tri-(2-CH3(CH2)10) phosphate,
tri-(3-CH3(CH2)10) phosphate, tri-(4-CH3(CH2)10) phosphate,
tri-(5-CH3(CH2)10) phosphate, tri-(1-CH3(CH2)11) phosphate,
tri-(2-CH3(CH2)11) phosphate, tri-(3-CH3(CH2)11) phosphate,
tri-(4-CH3(CH2)11) phosphate, tri-(5-CH3(CH2)11) phosphate,
tri-(6-CH3(CH2)11) phosphate, tri-(1-CH3(CH2)12) phosphate,
tri-(2-CH3(CH2)12) phosphate, tri-(3-CH3(CH2)12) phosphate,
tri-(4-CH3(CH2)12) phosphate, tri-(5-CH3(CH2)12) phosphate,
tri-(6-CH3(CH2)12) phosphate, tri-(methyl pentyl) phosphate,
tri-(ethyl pentyl) phosphate, tri-(methyl hexyl) phosphate,
tri-(ethyl hexyl) phosphate, tri-(propyl hexyl) phosphate,
tri-(methyl heptyl) phosphate, tri-(ethyl heptyl) phosphate,
tri-(diethyl heptyl) phosphate, tri-(methyl octyl) phosphate,
tri-(dimethyl octyl) phosphate, methyl di-(-ethyl) phosphate,
methyl di-(1-propyl) phosphate, methyl di-(2-propyl) phosphate,
methyl di-(1-butyl) phosphate, methyl di-(2-butyl) phosphate,
methyl di-(1-tert-butyl) phosphate, methyl di-(2-tert-butyl)
phosphate, methyl di-(1-pentyl) phosphate, methyl di-(2-pentyl)
phosphate, methyl di-(3-pentyl) phosphate, methyl di-(1-hexyl)
phosphate, methyl di-(2-hexyl) phosphate, methyl di-(3-hexyl)
phosphate, methyl di-(1-heptyl) phosphate, methyl di-(2-heptyl)
phosphate, methyl di-(3-heptyl) phosphate, methyl di-(4-heptyl)
phosphate, methyl di-(2-octyl) phosphate, methyl di-(2-octyl)
phosphate, methyl di-(3-octyl) phosphate, methyl di-(4-octyl)
phosphate, methyl di-(2-CH3(CH2)8) phosphate, methyl
di-(2-CH3(CH2)8) phosphate, methyl di-(3-CH3(CH2)8) phosphate,
methyl di-(4-CH3(CH2)8) phosphate, methyl di-(3-CH3(CH2)9)
phosphate, methyl di-(2-CH3(CH2)9) phosphate, methyl
di-(3-CH3(CH2)9) phosphate, methyl di-(4-CH3(CH2)9) phosphate,
methyl di-(5-CH3(CH2)9) phosphate, methyl di-(1-CH3(CH2)10)
phosphate, methyl di-(2-CH3(CH2)10) phosphate, methyl
di-(3-CH3(CH2)10) phosphate, methyl di-(4-CH3(CH2)10) phosphate,
methyl di-(5-CH3(CH2)10) phosphate, methyl di-(1-CH3(CH2)11)
phosphate, methyl di-(2-CH3(CH2)11) phosphate, methyl
di-(3-CH3(CH2)11) phosphate, methyl di-(4-CH3(CH2)11) phosphate,
methyl di-(5-CH3(CH2)11) phosphate, methyl di-(6-CH3(CH2)11)
phosphate, methyl di-(1-CH3(CH2)12) phosphate, methyl
di-(2-CH3(CH2)12) phosphate, methyl di-(3-CH3(CH2)12) phosphate,
methyl di-(4-CH3(CH2)12) phosphate, methyl di-(5-CH3(CH2)12)
phosphate, methyl di-(6-CH3(CH2)12) phosphate, ethyl di-(1-propyl)
phosphate, ethyl di-(2-propyl) phosphate, ethyl di-(1-butyl)
phosphate, ethyl di-(2-butyl) phosphate, ethyl di-(1-tert-butyl)
phosphate, ethyl di-(2-tert-butyl) phosphate, ethyl di-(1-pentyl)
phosphate, ethyl di-(2-pentyl) phosphate, ethyl di-(3-pentyl)
phosphate, ethyl di-(1-hexyl) phosphate, ethyl di-(2-hexyl)
phosphate, ethyl di-(3-hexyl) phosphate, ethyl di-(1-heptyl)
phosphate, ethyl di-(2-heptyl) phosphate, ethyl di-(3-heptyl)
phosphate, ethyl di-(4-heptyl) phosphate, ethyl di-(1-octyl)
phosphate, ethyl di-(2-octyl) phosphate, ethyl di-(3-octyl)
phosphate, ethyl di-(4-octyl) phosphate, ethyl di-(1-CH3(CH2)8)
phosphate, ethyl di-(2-CH3(CH2)8) phosphate, ethyl di-(3-CH3(CH2)8)
phosphate, ethyl di-(4-CH3(CH2)8) phosphate, ethyl di-(1-CH3(CH2)9)
phosphate, ethyl di-(2-CH3(CH2)9) phosphate, ethyl di-(3-CH3(CH2)9)
phosphate, ethyl di-(4-CH3(CH2)9) phosphate, ethyl di-(5-CH3(CH2)9)
phosphate, ethyl di-(1-CH3(CH2)10) phosphate, ethyl
di-(2-CH3(CH2)10) phosphate, ethyl di-(3-CH3(CH2)10) phosphate,
ethyl di-(4-CH3(CH2)10) phosphate, ethyl di-(5-CH3(CH2)10)
phosphate, ethyl di-(1-CH3(CH2)11) phosphate, ethyl
di-(2-CH3(CH2)11) phosphate, ethyl di-(3-CH3(CH2)11) phosphate,
ethyl di-(4-CH3(CH2)11) phosphate, ethyl di-(5-CH3(CH2)11)
phosphate, ethyl di-(6-CH3(CH2)11) phosphate, ethyl
di-(5-CH3(CH2)12) phosphate, ethyl di-(2-CH3(CH2)12) phosphate,
ethyl di-(3-CH3(CH2)12) phosphate, ethyl di-(4-CH3(CH2)12)
phosphate, ethyl di-(5-CH3(CH2)12) phosphate, ethyl
di-(6-CH3(CH2)12) phosphate, 1-propyl di-(2-propyl) phosphate,
1-propyl di-(1-butyl) phosphate, 1-propyl di-(2-butyl) phosphate,
1-propyl di-(1-tert-butyl) phosphate, 1-propyl di-(2-tert-butyl)
phosphate, 1-propyl di-(1-pentyl) phosphate, 1-propyl di-(2-pentyl)
phosphate, 1-propyl di-(3-pentyl) phosphate, 1-propyl di-(1-hexyl)
phosphate, 1-propyl di-(2-hexyl) phosphate, 1-propyl di-(3-hexyl)
phosphate, 1-propyl di-(1-heptyl) phosphate, 1-propyl di-(2-heptyl)
phosphate, 1-propyl di-(3-heptyl) phosphate, 1-propyl di-(4-heptyl)
phosphate, 1-propyl di-(1-octyl) phosphate, 1-propyl di-(2-octyl)
phosphate, 1-propyl di-(3-octyl) phosphate, 1-propyl di-(4-octyl)
phosphate, 1-propyl di-(1-CH3(CH2)8) phosphate, 1-propyl
di-(2-CH3(CH2)8) phosphate, 1-propyl di-(3-CH3(CH2)8) phosphate,
1-propyl di-(4-CH3(CH2)8) phosphate, 1-propyl di-(1-CH3(CH2)9)
phosphate, 1-propyl di-(2-CH3(CH2)9) phosphate, 1-propyl
di-(3-CH3(CH2)9) phosphate, 1-propyl di-(4-CH3(CH2)9) phosphate,
1-propyl di-(5-CH3(CH2)9) phosphate, 1-propyl di-(4-CH3(CH2)10)
phosphate, 1-propyl di-(2-CH3(CH2)10) phosphate, 1-propyl
di-(3-CH3(CH2)10) phosphate, 1-propyl di-(4-CH3(CH2)10) phosphate,
1-propyl di-(5-CH3(CH2)10) phosphate, 1-propyl di-(1-CH3(CH2)11)
phosphate, 1-propyl di-(2-CH3(CH2)11) phosphate, 1-propyl
di-(3-CH3(CH2)11) phosphate, 1-propyl di-(4-CH3(CH2)11) phosphate,
1-propyl di-(5-CH3(CH2)11) phosphate, 1-propyl di-(6-CH3(CH2)11)
phosphate, 1-propyl di-(1-CH3(CH2)12) phosphate, 1-propyl
di-(2-CH3(CH2)12) phosphate, 1-propyl di-(3-CH3(CH2)12) phosphate,
1-propyl di-(4-CH3(CH2)12) phosphate, 1-propyl di-(5-CH3(CH2)12)
phosphate, 1-propyl di-(6-CH3(CH2)12) phosphate, 2-propyl
di-(1-butyl) phosphate, 2-propyl di-(2-butyl) phosphate, 2-propyl
di-(1-tert-butyl) phosphate, 2-propyl di-(2-tert-butyl) phosphate,
2-propyl di-(1-pentyl) phosphate, 2-propyl di-(2-pentyl) phosphate,
2-propyl di-(3-pentyl) phosphate, 2-propyl di-(1-hexyl) phosphate,
2-propyl di-(2-hexyl) phosphate, 2-propyl di-(3-hexyl) phosphate,
2-propyl di-(1-heptyl) phosphate, 2-propyl di-(2-heptyl) phosphate,
2-propyl di-(3-heptyl) phosphate, 2-propyl di-(4-heptyl) phosphate,
2-propyl di-(1-octyl) phosphate, 2-propyl di-(2-octyl) phosphate,
2-propyl di-(3-octyl) phosphate, 2-propyl di-(4-octyl) phosphate,
2-propyl di-(1CH3(CH2)8) phosphate, 2-propyl di-(2-CH3(CH2)8)
phosphate, 2-propyl di-(3-CH3(CH2)8) phosphate, 2-propyl
di-(4-CH3(CH2)8) phosphate, 2-propyl di-(3-CH3(CH2)9) phosphate,
2-propyl di-(2-CH3(CH2)9) phosphate, 2-propyl di-(3-CH3(CH2)9)
phosphate, 2-propyl di-(4-CH3(CH2)9) phosphate, 2-propyl
di-(5-CH3(CH2)9) phosphate, 2-propyl di-(1-CH3(CH2)10) phosphate,
2-propyl di-(2-CH3(CH2)10) phosphate, 2-propyl di-(3-CH3(CH2)10)
phosphate, 2-propyl di-(4-CH3(CH2)10) phosphate, 2-propyl
di-(5-CH3(CH2)10) phosphate, 2-propyl di-(1-CH3(CH2)11) phosphate,
2-propyl di-(2-CH3(CH2)11) phosphate, 2-propyl di-(3-CH3(CH2)11)
phosphate, 2-propyl di-(4-CH3(CH2)11) phosphate, 2-propyl
di-(5-CH3(CH2)11) phosphate, 2-propyl di-(6-CH3(CH2)11) phosphate,
2-propyl di-(1-CH3(CH2)12) phosphate, 2-propyl di-(2-CH3(CH2)12)
phosphate, 2-propyl di-(3-CH3(CH2)12) phosphate, 2-propyl
di-(4-CH3(CH2)12) phosphate, 2-propyl di-(5-CH3(CH2)12) phosphate,
2-propyl di-(6-CH3(CH2)12) phosphate, butyl di-(1-tert-butyl)
phosphate, butyl di-(2-tert-butyl) phosphate, butyl di-(2-pentyl)
phosphate, butyl di-(2-pentyl) phosphate, butyl di-(3-pentyl)
phosphate, butyl di-(1-hexyl) phosphate, butyl di-(2-hexyl)
phosphate, butyl di-(3-hexyl) phosphate, butyl di-(1-heptyl)
phosphate, butyl di-(2-heptyl) phosphate, butyl di-(3-heptyl)
phosphate, butyl di-(4-heptyl) phosphate, butyl di-(1-octyl)
phosphate, butyl di-(2-octyl) phosphate, butyl di-(3-octyl)
phosphate, butyl di-(4-octyl) phosphate, butyl di-(1-CH3(CH2)8)
phosphate, butyl di-(2-CH3(CH2)8) phosphate, butyl di-(3-CH3(CH2)8)
phosphate, butyl di-(4-CH3(CH2)8) phosphate, butyl di-(1-CH3(CH2)9)
phosphate, butyl di-(2-CH3(CH2)9) phosphate, butyl di-(3-CH3(CH2)9)
phosphate, butyl di-(4-CH3(CH2)9) phosphate, butyl di-(5-CH3(CH2)9)
phosphate, butyl di-(1-CH3(CH2)10) phosphate, butyl
di-(2-CH3(CH2)10) phosphate, butyl di-(3-CH3(CH2)10) phosphate,
butyl di-(4-CH3(CH2)10) phosphate, butyl di-(5-CH3(CH2)10)
phosphate, butyl di-(1-CH3(CH2)11) phosphate, butyl
di-(2-CH3(CH2)11) phosphate, butyl di-(3-CH3(CH2)11) phosphate,
butyl di-(4-CH3(CH2)11) phosphate, butyl di-(5-CH3(CH2)11)
phosphate, butyl di-(6-CH3(CH2)11) phosphate, butyl
di-(1-CH3(CH2)12) phosphate, butyl di-(2-CH3(CH2)12) phosphate,
butyl di-(3-CH3(CH2)12) phosphate, butyl di-(4-CH3(CH2)12)
phosphate, butyl di-(5-CH3(CH2)12) phosphate, butyl
di-(6-CH3(CH2)12) phosphate, methyl ethyl propyl phosphate, methyl
ethyl butyl phosphate, methyl ethyl pentyl phosphate, methyl ethyl
hexyl phosphate, methyl ethyl heptyl phosphate, methyl ethyl octyl
phosphate, methyl propyl butyl phosphate, methyl propyl pentyl
phosphate, methyl propyl hexyl phosphate, methyl propyl heptyl
phosphate, methyl propyl octyl phosphate, methyl butyl pentyl
phosphate, methyl butyl hexyl phosphate, methyl butyl heptyl
phosphate, methyl butyl octyl phosphate, methyl pentyl hexyl
phosphate, methyl pentyl heptyl phosphate, methyl pentyl octyl
phosphate, methyl hexyl heptyl phosphate, methyl hexyl octyl
phosphate, ethyl propyl butyl phosphate, ethyl propyl pentyl
phosphate, ethyl propyl hexyl phosphate, ethyl propyl heptyl
phosphate, ethyl propyl octyl phosphate, ethyl butyl pentyl
phosphate, ethyl butyl hexyl phosphate, ethyl butyl heptyl
phosphate, ethyl butyl octyl phosphate, ethyl pentyl hexyl
phosphate, ethyl pentyl heptyl phosphate, ethyl pentyl octyl
phosphate, ethyl hexyl heptyl phosphate, ethyl hexyl octyl
phosphate, tri-phenyl phosphate, methyl di-phenyl phosphate, ethyl
di-phenyl phosphate, 1 propyl di-phenyl phosphate, 2 propyl
di-phenyl phosphate, 1 butyl di-phenyl phosphate, 2 butyl di-phenyl
phosphate, 1 tert-butyl di-phenyl phosphate, 2 tert-butyl di-phenyl
phosphate, 1 pentyl di-phenyl phosphate, 2 pentyl di-phenyl
phosphate, 3 pentyl di-phenyl phosphate, 1 hexyl di-phenyl
phosphate, 2 hexyl di-phenyl phosphate, 3 hexyl di-phenyl
phosphate, 1 heptyl di-phenyl phosphate, 2 heptyl di-phenyl
phosphate, 3 heptyl di-phenyl phosphate, 4 heptyl di-phenyl
phosphate, 1 octyl di-phenyl phosphate, 2 octyl di-phenyl
phosphate, 3 octyl di-phenyl phosphate, 4 octyl di-phenyl
phosphate, 1 CH3(CH2)8 di-phenyl phosphate, 2 CH3(CH2)8 di-phenyl
phosphate, 3 CH3(CH2)8 di-phenyl phosphate, 4 CH3(CH2)8 di-phenyl
phosphate, 1 CH3(CH2)9 di-phenyl phosphate, 2 CH3(CH2)9 di-phenyl
phosphate, 3 CH3(CH2)9 di-phenyl phosphate, 4 CH3(CH2)9 di-phenyl
phosphate, 5 CH3(CH2)9 di-phenyl phosphate, 1 CH3(CH2)10 di-phenyl
phosphate, 2 CH3(CH2)10 di-phenyl phosphate, 3 CH3(CH2)10 di-phenyl
phosphate, 4 CH3(CH2)10 di-phenyl phosphate, 5 CH3(CH2)10 di-phenyl
phosphate, 1 CH3(CH2)11 di-phenyl phosphate, 2 CH3(CH2)11 di-phenyl
phosphate, 3 CH3(CH2)11 di-phenyl phosphate, 4 CH3(CH2)11 di-phenyl
phosphate, 5 CH3(CH2)11 di-phenyl phosphate, 6 CH3(CH2)11 di-phenyl
phosphate, 1 CH3(CH2)12 di-phenyl phosphate, 2 CH3(CH2)12 di-phenyl
phosphate, 3 CH3(CH2)12 di-phenyl phosphate, 4 CH3(CH2)12 di-phenyl
phosphate, 5 CH3(CH2)12 di-phenyl phosphate, 6 CH3(CH2)12 di-phenyl
phosphate, di-methyl phenyl phosphate, di-ethyl phenyl phosphate,
di-(1-propyl) phenyl phosphate, di-(2-propyl) phenyl phosphate,
di-(-isopropyl) phenyl phosphate, di-(1-butyl) phenyl phosphate,
di-(2-butyl) phenyl phosphate, di-(l-tert-butyl) phenyl phosphate,
di-(2-tert-butyl) phenyl phosphate, di-(1-pentyl) phenyl phosphate,
di-(2-pentyl) phenyl phosphate, di-(3-pentyl) phenyl phosphate,
di-(1-hexyl) phenyl phosphate, di-(2-hexyl) phenyl phosphate,
di-(3-hexyl) phenyl phosphate, di-(1-heptyl) phenyl phosphate,
di-(2-heptyl) phenyl phosphate, di-(3-heptyl ) phenyl phosphate,
di-(4-heptyl) phenyl phosphate, di-(1-octyl) phenyl phosphate,
di-(2-octyl) phenyl phosphate, di-(3-octyl) phenyl phosphate,
di-(4-octyl) phenyl phosphate, di-(1-CH3(CH2)8) phenyl phosphate,
di-(2-CH3(CH2)8) phenyl phosphate, di-(3-CH3(CH2)8) phenyl
phosphate, di-(4-CH3(CH2)8) phenyl phosphate, di-(1-CH3(CH2)9)
phenyl phosphate, di-(2-CH3(CH2)9) phenyl phosphate,
di-(3-CH3(CH2)9) phenyl phosphate, di-(4-CH3(CH2)9) phenyl
phosphate, di-(5-CH3(CH2)9) phenyl phosphate, di-(1-CH3(CH2)10)
phenyl phosphate, di-(2-CH3(CH2)10) phenyl phosphate,
di-(3-CH3(CH2)10) phenyl phosphate, di-(4-CH3(CH2)10) phenyl
phosphate, di-(5-CH3(CH2)10) phenyl phosphate, di-(4-CH3(CH2)11)
phenyl phosphate, di-(2-CH3(CH2)10) phenyl phosphate,
di-(3-CH3(CH2)11) phenyl phosphate, di-(4-CH3(CH2)11) phenyl
phosphate, di-(5-CH3(CH2)11) phenyl phosphate, di-(6-CH3(CH2)11)
phenyl phosphate, di-(5-CH3(CH2)12) phenyl phosphate,
di-(2-CH3(CH2)12) phenyl phosphate, di-(3-CH3(CH2)12) phenyl
phosphate, di-(4-CH3(CH2)12) phenyl phosphate, di-(5-CH3(CH2)12)
phenyl phosphate, di-(6-CH3(CH2)12) phenyl phosphate, tri-ethylene
phosphate, tri-(1-propene) phosphate, tri-(2-propene) phosphate,
tri-(3-propene) phosphate, tri-(1-(1-butene)) phosphate,
tri-(2-(1-butene)) phosphate, tri-(3-(1-butene)) phosphate,
tri-(4-(1-butene)) phosphate, tri-(1-(2-butene)) phosphate,
tri-(2-(2-butene)) phosphate, tri-(3-(2-butene)) phosphate,
tri-(4-(2-butene)) phosphate, tri-(1-(1-pentene)) phosphate,
tri-(2-(1-pentene)) phosphate, tri-(3-(1-pentene)) phosphate,
tri-(4-(1-pentene)) phosphate, tri-(5-(1-pentene)) phosphate,
tri-(1-(2-pentene)) phosphate, tri-(2-(2-pentene)) phosphate,
tri-(3-(2-pentene)) phosphate, tri-(4-(2-pentene)) phosphate,
tri-(5-(2-pentyl)) phosphate, tri-(1-(1-hexene)) phosphate,
tri-(2-(1-hexene)) phosphate, tri-(3-(1-hexene)) phosphate,
tri-(4-(1-hexene)) phosphate, tri-(5-(1-hexene)) phosphate,
tri-(6-(1-hexene)) phosphate, tri-(1-(3-hexene)) phosphate,
tri-(2-(3-hexene)) phosphate, tri-(3-(3-hexene)) phosphate,
tri-(4-(3-hexene)) phosphate, tri-(5-(3-hexene)) phosphate,
tri-(6-(3-hexene)) phosphate, tri-(1-(2-hexene)) phosphate,
tri-(2-(2-hexene)) phosphate, tri-(3-(2-hexene)) phosphate,
tri-(4-(2-hexene)) phosphate, tri-(5-(2-hexene)) phosphate,
tri-(6-(2-hexene)) phosphate, tri-(phenyl methyl) phosphate,
tri-(2-methyl phenyl) phosphate, tri-(3-methyl phenyl) phosphate,
tri-(4-methyl phenyl) phosphate, tri-(2-ethyl phenyl) phosphate,
tri-(3-ethyl phenyl) phosphate, and tri-(4-ethyl phenyl)
phosphate.
Specific examples of di-phosphates include: di-methyl phosphate,
di-ethyl phosphate, di-(1-propyl) phosphate, di-(2-propyl)
phosphate, di-(1-butyl) phosphate, di-(2-butyl) phosphate,
di-(1-tert-butyl) phosphate, di-(2-tert-butyl) phosphate,
di-(1-pentyl) phosphate, di-(2-pentyl) phosphate, di-(3-pentyl)
phosphate, di-(1-hexyl) phosphate, di-(2-hexyl) phosphate,
di-(3-hexyl) phosphate, di-(1-heptyl) phosphate, di-(2-heptyl)
phosphate, di-(3-heptyl) phosphate, di-(4-heptyl) phosphate,
di-(1-octyl) phosphate, di-(2-octyl) phosphate, di-(3-octyl)
phosphate, di-(4-octyl) phosphate, di-(1-CH3(CH2)8) phosphate,
di-(2-CH3(CH2)8) phosphate, di-(3-CH3(CH2)8) phosphate,
di-(4-CH3(CH2)8) phosphate, di-(1-CH3(CH2)9) phosphate,
di-(2-CH3(CH2)9) phosphate, di-(3-CH3(CH2)9) phosphate,
di-(4-CH3(CH2)9) phosphate, di-(5-CH3(CH2)9) phosphate,
di-(1-CH3(CH2)10) phosphate, di-(2-CH3(CH2)10) phosphate,
di-(3-CH3(CH2)10) phosphate, di-(4-CH3(CH2)10) phosphate,
di-(5-CH3(CH2)10) phosphate, di-(1-CH3(CH2)11) phosphate,
di-(2-CH3(CH2)11) phosphate, di-(3-CH3(CH2)11) phosphate,
di-(4-CH3(CH2)11) phosphate, di-(5-CH3(CH2)11) phosphate,
di-(6-CH3(CH2)11) phosphate, di-(1-CH3(CH2)12) phosphate,
di-(2-CH3(CH2)12) phosphate, di-(3-CH3(CH2)12) phosphate,
di-(4-CH3(CH2)12) phosphate, di-(5-CH3(CH2)12) phosphate,
di-(6-CH3(CH2)12) phosphate, di-(1-(methyl pentyl)) phosphate,
di-(2-(methyl pentyl)) phosphate, di-(3-(methyl pentyl)) phosphate,
di-(1-(di-methyl pentyl)) phosphate, di-(2-(di-methyl pentyl))
phosphate, di-(3-(di-methyl pentyl)) phosphate, di-(1-(ethyl
pentyl)) phosphate, di-(2-(ethyl pentyl)) phosphate, di-(3-(ethyl
pentyl)) phosphate, di-(1-(methyl hexyl)) phosphate, di-(2-(methyl
hexyl)) phosphate, di-(3-(methyl hexyl)) phosphate,
di-(1-(di-methyl hexyl)) phosphate, di-(2-(di-methyl hexyl))
phosphate, di-(3-(di-methyl hexyl)) phosphate, di-(1-(ethyl hexyl))
phosphate, di-(2-(ethyl hexyl)) phosphate, di-(3-(ethyl hexyl))
phosphate, di-(methyl heptyl) phosphate, di-(di-methyl heptyl)
phosphate, di-(ethyl heptyl) phosphate, di-(methyl octyl)
phosphate, di-(di-methyl octyl) phosphate, di-(ethyl octyl)
phosphate, methyl ethyl phosphate, methyl propyl phosphate, methyl
butyl phosphate, methyl tert-butyl phosphate, methyl pentyl
phosphate, methyl hexyl phosphate, methyl heptyl phosphate, methyl
octyl phosphate, methyl CH3(CH2)8 phosphate, methyl CH3(CH2)9
phosphate, methyl CH3(CH2)10 phosphate, methyl CH3(CH2)11
phosphate, methyl CH3(CH2)12 phosphate, ethyl propyl phosphate,
ethyl butyl phosphate, ethyl tert-butyl phosphate, ethyl pentyl
phosphate, ethyl hexyl phosphate, ethyl heptyl phosphate, ethyl
octyl phosphate, ethyl CH3(CH2)8 phosphate, ethyl CH3(CH2)9
phosphate, ethyl CH3(CH2)10 phosphate, ethyl CH3(CH2)11 phosphate,
ethyl CH3(CH2)12 phosphate, propyl butyl phosphate, propyl
tert-butyl phosphate, propyl pentyl phosphate, propyl hexyl
phosphate, propyl heptyl phosphate, propyl octyl phosphate, propyl
CH3(CH2)8 phosphate, propyl CH3(CH2)9 phosphate, propyl CH3(CH2)10
phosphate, propyl CH3(CH2)11 phosphate, propyl CH3(CH2)12
phosphate, butyl tert-butyl phosphate, tert-butyl pentyl phosphate,
tert-butyl hexyl phosphate, tert-butyl heptyl phosphate, tert-butyl
octyl phosphate, tert-butyl CH3(CH2)8 phosphate, tert-butyl
CH3(CH2)9 phosphate, tert-butyl CH3(CH2)10 phosphate, tert-butyl
CH3(CH2)11 phosphate, tert-butyl CH3(CH2)12 phosphate, pentyl hexyl
phosphate, pentyl heptyl phosphate, pentyl octyl phosphate, pentyl
CH3(CH2)8 phosphate, pentyl CH3(CH2)9 phosphate, pentyl CH3(CH2)10
phosphate, pentyl CH3(CH2)11 phosphate, pentyl CH3(CH2)12
phosphate, hexyl heptyl phosphate, hexyl octyl phosphate, hexyl
CH3(CH2)8 phosphate, hexyl CH3(CH2)9 phosphate, hexyl CH3(CH2)10
phosphate, hexyl CH3(CH2)11 phosphate, hexyl CH3(CH2)12 phosphate,
di-butene phosphate, di-pentene phosphate, di-hexene phosphate,
di-heptene phosphate, and di-octene phosphate.
Specific examples of mono-phosphates include: methyl phosphate,
ethyl phosphate, propyl phosphate, butyl phosphate, pentyl
phosphate, hexyl phosphate, heptyl phosphate, octyl phosphate,
CH3(CH2)8 phosphate, CH3(CH2)9 phosphate, CH3(CH2)10 phosphate,
CH3(CH2)11 phosphate, CH3(CH2)12 phosphate, methyl propyl
phosphate, methyl butyl phosphate, methyl pentyl phosphate, methyl
hexyl phosphate, methyl heptyl phosphate, methyl octyl phosphate,
methyl CH3(CH2)8 phosphate, methyl CH3(CH2)9 phosphate, methyl
CH3(CH2)10 phosphate, methyl CH3(CH2)11 phosphate, methyl
CH3(CH2)12 phosphate, di-methyl butyl phosphate, di-methyl pentyl
phosphate, di-methyl hexyl phosphate, di-methyl heptyl phosphate,
di-methyl octyl phosphate, di-methyl CH3(CH2)8 phosphate, di-methyl
CH3(CH2)9 phosphate, di-methyl CH3(CH2)10 phosphate, di-methyl
CH3(CH2)11 phosphate, di-methyl CH3(CH2)12 phosphate, ethyl butyl
phosphate, ethyl pentyl phosphate, ethyl hexyl phosphate, ethyl
heptyl phosphate, ethyl octyl phosphate, ethyl CH3(CH2)8 phosphate,
ethyl CH3(CH2)9 phosphate, ethyl CH3(CH2)10 phosphate, ethyl
CH3(CH2)11 phosphate, ethyl CH3(CH2)12 phosphate, butene phosphate,
pentene phosphate, hexene phosphate, heptene phosphate, and octene
phosphate.
For purposes of brevity, a complete list of phosphites is not
provided; however, applicable phosphite species correspond to the
each of the tri, di, and mono phosphates provided in the preceding
paragraphs. For example, by simply replacing the word "phosphate"
with "phosphite" in the preceding paragraphs, one can quickly
generate a list of representative phosphite species applicable to
the subject invention.
Examples of phosphine compounds include: tri-(1-hexyl) phosphine,
tri-(2-hexyl) phosphine, tri-(3-hexyl) phosphine, tri-(4-heptyl)
phosphine, tri-(2-heptyl) phosphine, tri-(3-heptyl) phosphine,
tri-(4-heptyl) phosphine, tri-(1-octyl) phosphine, tri-(2-octyl)
phosphine, tri-(3-octyl) phosphine, tri-(4-octyl) phosphine,
tri-(1-CH3(CH2)8) phosphine, tri-(2-CH3(CH2)8) phosphine,
tri-(3-CH3(CH2)8) phosphine, tri-(4-CH3(CH2)8) phosphine,
tri-(1-CH3(CH2)9) phosphine, tri-(2-CH3(CH2)9) phosphine,
tri-(3-CH3(CH2)9) phosphine, tri-(4-CH3(CH2)9) phosphine,
tri-(5-CH3(CH2)9) phosphine, tri-(1-CH3(CH2)10) phosphine,
tri-(2-CH3(CH2)10) phosphine, tri-(3-CH3(CH2)10) phosphine,
tri-(4-CH3(CH2)10) phosphine, tri-(5-CH3(CH2)10) phosphine,
tri-(1-CH3(CH2)11) phosphine, tri-(2-CH3(CH2)11) phosphine,
tri-(3-CH3(CH2)11) phosphine, tri-(4-CH3(CH2)11) phosphine,
tri-(5-CH3(CH2)11) phosphine, tri-(6-CH3(CH2)11) phosphine,
tri-(1-CH3(CH2)12) phosphine, tri-(2-CH3(CH2)12) phosphine,
tri-(3-CH3(CH2)12) phosphine, tri-(4-CH3(CH2)12) phosphine,
tri-(5-CH3(CH2)12) phosphine, tri-(6-CH3(CH2)12) phosphine, methyl
di-(1-hexyl) phosphine, methyl di-(2-hexyl) phosphine, methyl
di-(3-hexyl) phosphine, methyl di-(1-heptyl) phosphine, methyl
di-(2-heptyl) phosphine, methyl di-(3-heptyl) phosphine, methyl
di-(4-heptyl) phosphine, methyl di-(1-octyl) phosphine, methyl
di-(2-octyl) phosphine, methyl di-(3-octyl) phosphine, methyl
di-(4-octyl) phosphine, methyl di-(1-CH3(CH2)8) phosphine, methyl
di-(2-CH3(CH2)8) phosphine, methyl di-(3-CH3(CH2)8) phosphine,
methyl di-(4-CH3(CH2)8) phosphine, methyl di-(1-CH3(CH2)9)
phosphine, methyl di-(2-CH3(CH2)9) phosphine, methyl
di-(3-CH3(CH2)9) phosphine, methyl di-(4-CH3(CH2)9) phosphine,
methyl di-(5-CH3(CH2)9) phosphine, methyl di-(1-CH3(CH2)10)
phosphine, methyl di-(2-CH3(CH2)10) phosphine, methyl
di-(3-CH3(CH2)10) phosphine, methyl di-(4-CH3(CH2)10) phosphine,
methyl di-(5-CH3(CH2)10) phosphine, methyl di-(1-CH3(CH2)11)
phosphine, methyl di-(2-CH3(CH2)11) phosphine, methyl
di-(3-CH3(CH2)11) phosphine, methyl di-(4-CH3(CH2)11) phosphine,
methyl di-(5-CH3(CH2)11) phosphine, methyl di-(6-CH3(CH2)11)
phosphine, methyl di-(1-CH3(CH2)12) phosphine, methyl
di-(2-CH3(CH2)12) phosphine, methyl di-(3-CH3(CH2)12) phosphine,
methyl di-(4-CH3(CH2)12) phosphine, methyl di-(5-CH3(CH2)12)
phosphine, methyl di-(6-CH3(CH2)12) phosphine, ethyl di-(1-hexyl)
phosphine, ethyl di-(2-hexyl) phosphine, ethyl di-(3-hexyl)
phosphine, ethyl di-(1-heptyl) phosphine, ethyl di-(2-heptyl)
phosphine, ethyl di-(3-heptyl) phosphine, ethyl di-(4-heptyl)
phosphine, ethyl di-(1-octyl) phosphine, ethyl di-(2-octyl)
phosphine, ethyl di-(3-octyl) phosphine, ethyl di-(4-octyl)
phosphine, ethyl di-(1-CH3(CH2)8) phosphine, ethyl di-(2-CH3(CH2)8)
phosphine, ethyl di-(3-CH3(CH2)8) phosphine, ethyl di-(4-CH3(CH2)8)
phosphine, ethyl di-(1-CH3(CH2)9) phosphine, ethyl di-(2-CH3(CH2)9)
phosphine, ethyl di-(3-CH3(CH2)9) phosphine, ethyl di-(4-CH3(CH2)9)
phosphine, ethyl di-(5-CH3(CH2)9) phosphine, ethyl
di-(1-CH3(CH2)10) phosphine, ethyl di-(2-CH3(CH2)10) phosphine,
ethyl di-(3-CH3(CH2)10) phosphine, ethyl di-(4-CH3(CH2)10)
phosphine, ethyl di-(5-CH3(CH2)10) phosphine, ethyl
di-(1-CH3(CH2)10) phosphine, ethyl di-(2-CH3(CH2)11) phosphine,
ethyl di-(3-CH3(CH2)1) phosphine, ethyl di-(4-CH3(CH2)10)
phosphine, ethyl di-(5-CH3(CH2)11) phosphine, ethyl
di-(6-CH3(CH2)11) phosphine, ethyl di-(1-CH3(CH2)12) phosphine,
ethyl di-(2-CH3(CH2)12) phosphine, ethyl di-(3-CH3(CH2)12)
phosphine, ethyl di-(4-CH3(CH2)12) phosphine, ethyl
di-(5-CH3(CH2)12) phosphine, ethyl di-(6-CH3(CH2)12) phosphine,
1-propyl di-(1-hexyl) phosphine, 1-propyl di-(2-hexyl) phosphine,
1-propyl di-(3-hexyl) phosphine, 1-propyl di-(1-heptyl) phosphine,
1-propyl di-(2-heptyl) phosphine, 1-propyl di-(3-heptyl) phosphine,
1-propyl di-(4-heptyl) phosphine, 1-propyl di-(1-octyl) phosphine,
1-propyl di-(2-octyl) phosphine, 1-propyl di-(3-octyl) phosphine,
1-propyl di-(4-octyl) phosphine, 1-propyl di-(1-CH3(CH2)8)
phosphine, 1-propyl di-(2-CH3(CH2)8) phosphine, 1-propyl
di-(3-CH3(CH2)8) phosphine, 1-propyl di-(4-CH3(CH2)8) phosphine,
1-propyl di-(1-CH3(CH2)9) phosphine, 1-propyl di-(2-CH3(CH2)9)
phosphine, 1-propyl di-(3-CH3(CH2)9) phosphine, 1-propyl
di-(4-CH3(CH2)9) phosphine, 1-propyl di-(5-CH3(CH2)9) phosphine,
1-propyl di-(1-CH3(CH2)10) phosphine, 1-propyl di-(2-CH3(CH2)10)
phosphine, 1-propyl di-(3-CH3(CH2)10) phosphine, 1-propyl
di-(4-CH3(CH2)10) phosphine, 1-propyl di-(5-CH3(CH2)10) phosphine,
1-propyl di-(1-CH3(CH2)11) phosphine, 1-propyl di-(2-CH3(CH2)11)
phosphine, 1-propyl di-(3-CH3(CH2)11) phosphine, 1-propyl
di-(4-CH3(CH2)11) phosphine, 1-propyl di-(5-CH3(CH2)11) phosphine,
1-propyl di-(6-CH3(CH2)11) phosphine, 1-propyl di-(1-CH3(CH2)12)
phosphine, 1-propyl di-(2-CH3(CH2)12) phosphine, 1-propyl
di-(3-CH3(CH2)12) phosphine, 1-propyl di-(4-CH3(CH2)12) phosphine,
1-propyl di-(5-CH3(CH2)12) phosphine, 1-propyl di-(6-CH3(CH2)12)
phosphine, 2-propyl di-(1-hexyl) phosphine, 2-propyl di-(2-hexyl)
phosphine, 2-propyl di-(3-hexyl) phosphine, 2-propyl di-(1-heptyl)
phosphine, 2-propyl di-(2-heptyl) phosphine, 2-propyl di-(3-heptyl)
phosphine, 2-propyl di-(4-heptyl) phosphine, 2-propyl di-(1-octyl)
phosphine, 2-propyl di-(2-octyl) phosphine, 2-propyl di-(3-octyl)
phosphine, 2-propyl di-(4-octyl) phosphine, 2-propyl
di-(1-CH3(CH2)8) phosphine, 2-propyl di-(2-CH3(CH2)8) phosphine,
2-propyl di-(3-CH3(CH2)8) phosphine, 2-propyl di-(4-CH3(CH2)8)
phosphine, 2-propyl di-(1-CH3(CH2)9) phosphine, 2-propyl
di-(2-CH3(CH2)9) phosphine, 2-propyl di-(3-CH3(CH2)9) phosphine,
2-propyl di-(4-CH3(CH2)9) phosphine, 2-propyl di-(5-CH3(CH2)9)
phosphine, 2-propyl di-(1-CH3(CH2)10) phosphine, 2-propyl
di-(2-CH3(CH2)10) phosphine, 2-propyl di-(3-CH3(CH2)10) phosphine,
2-propyl di-(4-CH3(CH2)10) phosphine, 2-propyl di-(5-CH3(CH2)10)
phosphine, 2-propyl di-(1-CH3(CH2)11) phosphine, 2-propyl
di-(2-CH3(CH2)11) phosphine, 2-propyl di-(3-CH3(CH2)11) phosphine,
2-propyl di-(4-CH3(CH2)11) phosphine, 2-propyl di-(5-CH3(CH2)11)
phosphine, 2-propyl di-(6-CH3(CH2)11) phosphine, 2-propyl
di-(1-CH3(CH2)12) phosphine, 2-propyl di-(2-CH3(CH2)12) phosphine,
2-propyl di-(3-CH3(CH2)12) phosphine, 2-propyl di-(4-CH3(CH2)12)
phosphine, 2-propyl di-(5-CH3(CH2)12) phosphine, 2-propyl
di-(6-CH3(CH2)12) phosphine, butyl di-(1-hexyl) phosphine, butyl
di-(2-hexyl) phosphine, butyl di-(3-hexyl) phosphine, butyl
di-(1-heptyl) phosphine, butyl di-(2-heptyl) phosphine, butyl
di-(3-heptyl) phosphine, butyl di-(4-heptyl) phosphine, butyl
di-(1-octyl) phosphine, butyl di-(2-octyl) phosphine, butyl
di-(3-octyl) phosphine, butyl di-(4-octyl) phosphine, butyl
di-(1-CH3(CH2)8) phosphine, butyl di-(2-CH3(CH2)8) phosphine, butyl
di-(3-CH3(CH2)8) phosphine, butyl di-(4-CH3(CH2)8) phosphine, butyl
di-(1-CH3(CH2)9) phosphine, butyl di-(2-CH3(CH2)9) phosphine, butyl
di-(3-CH3(CH2)9) phosphine, butyl di-(4-CH3(CH2)9) phosphine, butyl
di-(5-CH3(CH2)9) phosphine, butyl di-(1-CH3(CH2)10) phosphine,
butyl di-(2-CH3(CH2)10) phosphine, butyl di-(3-CH3(CH2)10)
phosphine, butyl di-(4-CH3(CH2)10) phosphine, butyl
di-(5-CH3(CH2)10) phosphine, butyl di-(1-CH3(CH2)11) phosphine,
butyl di-(2-CH3(CH2)11) phosphine, butyl di-(3-CH3(CH2)11)
phosphine, butyl di-(4-CH3(CH2)11) phosphine, butyl
di-(5-CH3(CH2)11) phosphine, butyl di-(6-CH3(CH2)11) phosphine,
butyl di-(1-CH3(CH2)12) phosphine, butyl di-(2-CH3(CH2)12)
phosphine, butyl di-(3-CH3(CH2)12) phosphine, butyl
di-(4-CH3(CH2)12) phosphine, butyl di-(5-CH3(CH2)12) phosphine,
butyl di-(6-CH3(CH2)12) phosphine, methyl hexyl heptyl phosphine,
methyl hexyl octyl phosphine, ethyl propyl butyl phosphine, ethyl
propyl pentyl phosphine, ethyl propyl hexyl phosphine, ethyl propyl
heptyl phosphine, ethyl propyl octyl phosphine, ethyl butyl pentyl
phosphine, ethyl butyl hexyl phosphine, ethyl butyl heptyl
phosphine, ethyl butyl octyl phosphine, ethyl pentyl hexyl
phosphine, ethyl pentyl heptyl phosphine, ethyl pentyl octyl
phosphine, ethyl hexyl heptyl phosphine, ethyl hexyl octyl
phosphine, tri-phenyl phosphine, 1 hexyl di-phenyl phosphine, 2
hexyl di-phenyl phosphine, 3 hexyl di-phenyl phosphine, 1 heptyl
di-phenyl phosphine, 2 heptyl di-phenyl phosphine, 3 heptyl
di-phenyl phosphine, 4 heptyl di-phenyl phosphine, 1 octyl
di-phenyl phosphine, 2 octyl di-phenyl phosphine, 3 octyl di-phenyl
phosphine, 4 octyl di-phenyl phosphine, 1 CH3(CH2)8 di-phenyl
phosphine, 2 CH3(CH2)8 di-phenyl phosphine, 3 CH3(CH2)8 di-phenyl
phosphine, 4 CH3(CH2)8 di-phenyl phosphine, 1 CH3(CH2)9 di-phenyl
phosphine, 2 CH3(CH2)9 di-phenyl phosphine, 3 CH3(CH2)9 di-phenyl
phosphine, 4 CH3(CH2)9 di-phenyl phosphine, 5 CH3(CH2)9 di-phenyl
phosphine, 1 CH3(CH2)10 di-phenyl phosphine, 2 CH3(CH2)10 di-phenyl
phosphine, 3 CH3(CH2)10 di-phenyl phosphine, 4 CH3(CH2)10 di-phenyl
phosphine, 5 CH3(CH2)10 di-phenyl phosphine, 1 CH3(CH2)11 di-phenyl
phosphine, 2 CH3(CH2)11 di-phenyl phosphine, 3 CH3(CH2)11 di-phenyl
phosphine, 4 CH3(CH2)11 di-phenyl phosphine, 5 CH3(CH2)11 di-phenyl
phosphine, 6 CH3(CH2)11 di-phenyl phosphine, 1 CH3(CH2)12 di-phenyl
phosphine, 2 CH3(CH2)12 di-phenyl phosphine, 3 CH3(CH2)12 di-phenyl
phosphine, 4 CH3(CH2)12 di-phenyl phosphine, 5 CH3(CH2)12 di-phenyl
phosphine, 6 CH3(CH2)12 di-phenyl phosphine, di-(1-hexyl) phenyl
phosphine, di-(2-hexyl) phenyl phosphine, di-(3-hexyl) phenyl
phosphine, di-(1-heptyl) phenyl phosphine, di-(2-heptyl) phenyl
phosphine, di-(3-heptyl) phenyl phosphine, di-(4-heptyl) phenyl
phosphine, di-(1-octyl) phenyl phosphine, di-(2-octyl) phenyl
phosphine, di-(3-octyl) phenyl phosphine, di-(4-octyl) phenyl
phosphine, di-(1-CH3(CH2)8) phenyl phosphine, di-(2-CH3(CH2)8)
phenyl phosphine, di-(3-CH3(CH2)8) phenyl phosphine,
di-(4-CH3(CH2)8) phenyl phosphine, di-(1-CH3(CH2)9) phenyl
phosphine, di-(2-CH3(CH2)9) phenyl phosphine, di-(3-CH3(CH2)9)
phenyl phosphine, di-(4-CH3(CH2)9) phenyl phosphine,
di-(5-CH3(CH2)9) phenyl phosphine, di-(1-CH3(CH2)10) phenyl
phosphine, di-(2-CH3(CH2)10) phenyl phosphine, di-(3-CH3(CH2)10)
phenyl phosphine, di-(4-CH3(CH2)10) phenyl phosphine,
di-(5-CH3(CH2)10) phenyl phosphine, di-(1-CH3(CH2)11) phenyl
phosphine, di-(2-CH3(CH2)11) phenyl phosphine, di-(3-CH3(CH2)11)
phenyl phosphine, di-(4-CH3(CH2)11) phenyl phosphine,
di-(5-CH3(CH2)11) phenyl phosphine, di-(6-CH3(CH2)11) phenyl
phosphine, di-(1-CH3(CH2)12) phenyl phosphine, di-(2-CH3(CH2)12)
phenyl phosphine, di-(3-CH3(CH2)12) phenyl phosphine,
di-(4-CH3(CH2)12) phenyl phosphine, di-(5-CH3(CH2)12) phenyl
phosphine, di-(6-CH3(CH2)12) phenyl phosphine, tri-(phenyl methyl)
phosphine, tri-(2-methyl phenyl) phosphine, tri-(3-methyl phenyl)
phosphine, tri-(4-methyl phenyl) phosphine, tri-(2-ethyl phenyl)
phosphine, tri-(3-ethyl phenyl) phosphine, tri-(4-ethyl phenyl)
phosphine, tri-(hexene) phosphine, tri-(heptene) phosphine,
tri-(octene) phosphine, tri-(heptyl) phosphine, tri-(heptyl)
phosphine, tri-(heptyl) phosphine, and tri-(heptyl) phosphine.
Examples of the phosphine oxides correspond to each of the
above-listed phosphines. A listing of such oxides can be quickly
generated by simply adding the word "oxides" to each of the above
listed phosphine species.
Examples of di-phosphonates include: tetra-methyl di-phosphonate,
tetra-ethyl di-phosphonate, tetra-(1-propyl) di-phosphonate,
tetra-(2-propyl) di-phosphonate, tetra-(1-butyl) di-phosphonate,
tetra-(2-butyl) di-phosphonate, tetra-(1-tert-butyl)
di-phosphonate, tetra-(2-tert-butyl) di-phosphonate,
tetra-(1-pentyl) di-phosphonate, tetra-(2-pentyl) di-phosphonate,
tetra-(3-pentyl) di-phosphonate, tetra-(1-hexyl) di-phosphonate,
tetra-(2-hexyl) di-phosphonate, tetra-(3-hexyl) di-phosphonate,
tetra-(1-heptyl) di-phosphonate, tetra-(2-heptyl) di-phosphonate,
tetra-(3-heptyl) di-phosphonate, tetra-(4-heptyl) di-phosphonate,
tetra-(1-octyl) di-phosphonate, tetra-(2-octyl) di-phosphonate,
tetra-(3-octyl) di-phosphonate, tetra-(4-octyl) di-phosphonate,
tetra-(1-CH3(CH2)8) di-phosphonate, tetra-(2-CH3(CH2)8)
di-phosphonate, tetra-(3-CH3(CH2)8) di-phosphonate,
tetra-(4-CH3(CH2)8) di-phosphonate, tetra-(1-CH3(CH2)9)
di-phosphonate, tetra-(2-CH3(CH2)9) di-phosphonate,
tetra-(3-CH3(CH2)9) di-phosphonate, tetra-(4-CH3(CH2)9)
di-phosphonate, tetra-(5-CH3(CH2)9) di-phosphonate,
tetra-(1-CH3(CH2)10) di-phosphonate, tetra-(2-CH3(CH2)10)
di-phosphonate, tetra-(3-CH3(CH2)10) di-phosphonate,
tetra-(4-CH3(CH2)10) di-phosphonate, tetra-(5-CH3(CH2)10)
di-phosphonate, tetra-(1-CH3(CH2)11) di-phosphonate,
tetra-(2-CH3(CH2)11) di-phosphonate, tetra-(3-CH3(CH2)11)
di-phosphonate, tetra-(4-CH3(CH2)11) di-phosphonate,
tetra-(5-CH3(CH2)11) di-phosphonate, tetra-(6-CH3(CH2)11)
di-phosphonate, tetra-(1-CH3(CH2)12) di-phosphonate,
tetra-(2-CH3(CH2)12) di-phosphonate, tetra-(3-CH3(CH2)12)
di-phosphonate, tetra-(4-CH3(CH2)12) di-phosphonate,
tetra-(5-CH3(CH2)12) di-phosphonate, tetra-(6-CH3(CH2)12)
di-phosphonate, tetra-phenyl di-phosphonate, di-methyl-(di-ethyl)
di-phosphonate, di-methyl-(di-phenyl) di-phosphonate, and
di-methyl-(di-4-pentene) di-phosphonate.
Examples of pyrophosphate compounds include: tetra-methyl
pyrophosphate, tetra-ethyl pyrophosphate, tetra-(1-propyl)
pyrophosphate, tetra-(2-propyl) pyrophosphate, tetra-(1-butyl)
pyrophosphate, tetra-(2-butyl) pyrophosphate, tetra-(1-tert-butyl)
pyrophosphate, tetra-(2-tert-butyl) pyrophosphate, tetra-(1-pentyl)
pyrophosphate, tetra-(2-pentyl) pyrophosphate, tetra-(3-pentyl)
pyrophosphate, tetra-(1-hexyl) pyrophosphate, tetra-(2-hexyl)
pyrophosphate, tetra-(3-hexyl) pyrophosphate, tetra-(1-heptyl)
pyrophosphate, tetra-(2-heptyl) pyrophosphate, tetra-(3-heptyl)
pyrophosphate, tetra-(4-heptyl) pyrophosphate, tetra-(1-octyl)
pyrophosphate, tetra-(2-octyl) pyrophosphate, tetra-(3-octyl)
pyrophosphate, tetra-(4-octyl) pyrophosphate, tetra-(1-CH3(CH2)8)
pyrophosphate, tetra-(2-CH3(CH2)8) pyrophosphate,
tetra-(3-CH3(CH2)8) pyrophosphate, tetra-(4-CH3(CH2)8)
pyrophosphate, tetra-(1-CH3(CH2)9) pyrophosphate,
tetra-(2-CH3(CH2)9) pyrophosphate, tetra-(3-CH3(CH2)9)
pyrophosphate, tetra-(4-CH3(CH2)9) pyrophosphate,
tetra-(5-CH3(CH2)9) pyrophosphate, tetra-(1-CH3(CH2)10)
pyrophosphate, tetra-(2-CH3(CH2)10) pyrophosphate,
tetra-(3-CH3(CH2)10) pyrophosphate, tetra-(4-CH3(CH2)10)
pyrophosphate, tetra-(5-CH3(CH2)10) pyrophosphate,
tetra-(1-CH3(CH2)11) pyrophosphate, tetra-(2-CH3(CH2)11)
pyrophosphate, tetra-(3-CH3(CH2)11) pyrophosphate,
tetra-(4-CH3(CH2)11) pyrophosphate, tetra-(5-CH3(CH2)11)
pyrophosphate, tetra-(6-CH3(CH2)11) pyrophosphate,
tetra-(1-CH3(CH2)12) pyrophosphate, tetra-(2-CH3(CH2)12)
pyrophosphate, tetra-(3-CH3(CH2)12) pyrophosphate,
tetra-(4-CH3(CH2)12) pyrophosphate, tetra-(5-CH3(CH2)12)
pyrophosphate, tetra-(6-CH3(CH2)12) pyrophosphate, tetra-phenyl
pyrophosphate, di-methyl-(di-ethyl) pyrophosphate,
di-methyl-(di-phenyl) pyrophosphate, and di-methyl-(di-4-pentene)
pyrophosphate.
Examples of additional phosphorous containing compounds include
those described in "Phosphorus Chemistry in Everyday Living" by A.
Toy and E. Walsh (second edition, 1987, ACS, Washington, DC.
Examples include: pyrophosphates, phosphonites, phosphorothioates,
phosphonothioates, phosphonates, phosphorodithioates,
bis-phosphorodithioates, phosphonodithioates,
phosphoramidothioates, and pyrophosphoramide. Specific species
include: tetra-propyl dithiono-pyrophosphate, tetra-ethyl
dithiono-pyrophosphate, O-ethyl O-[2-(di-isopropyl
amino)ethyl]methylphosphonite, O,O-dimethyl O-p-nitrohenyl
phosphorothioate, O,O-diethyl O-p-nitrophenyl phosphorothioate,
O,O-dimethyl O-(4-nitro-m-tolyl) phosphorothioate, O-ethyl
O-p-nitrophenyl phenylphosphono-thioate, O,O-diethyl
O-(3,5,6-trichloro-2-pyridyl) phosphorothioate, O,O-diethyl
O-(2-isopropyl-6-methyl-4-pyrimidinyl) phosphorothioate,
O,O-diethyl O-[4-methylsulfinyl)phenyl]phosphorothioate,
O,O-dimethyl O-[3-methyl-4-(methyl thio)phenyl]phosphorothioate,
O,O-dimethyl (2,2,2-trichloro-1-hydroxy-ethyl) phosphonate,
2,2-di-chlorovinyl di-methyl phosphate,
1,2-di-bromo-2,2-di-chloroethyl dimethyl phosphate,
2-chloro-1-(2,3,4-trichloro-phenyl)vinyl dimethyl phosphate,
O-(4-bromo-2-chloro-phenyl) O-ethyl S-propyl phosphoro-thioate,
O-ethyl-O-[4-(methyl-thio)phenyl]S-propyl phosphorodithioate,
O-ethyl S,S-di-propyl phosphorodithioate, diethyl
mercapto-succinate, S-ester with O,O-dimethyl phosphorodithioate,
S-[(1,1-dimethyl-ethyl)-thio]methyl]O,O-di ethyl
phosphorodithioate, O,O-dimethyl S-phthalimido-methyl
phosphorodithoate, O,O-dimethyl S-4-oxo-1,2,3-benzotriazin
3(4H)-ylmethyl phosphorodithioate, O,O,O',O'"-tetraethyl
S,S'-methlene bis-phosphorodithioate,
S-[(6-chloro-2-oxo-3-(2H)-benzoxazolyl)methyl]O,O-di-ethyl
phosphorodithionate, S-[(p-chlorophenyl-thio)methyl]O,O-diethyl
phosphorodithioate, 1,4-p-dioxane-2,3,-di-thiol S,S-bis(O,O-diethyl
phosphorodithioate, O-ethyl S-phenyl Ethyl-phosphonodithioate,
O,S-dimethyl phosphoramidothioate, O,S-dimethyl
acetyl-phosphoramidothioate, 1-methylethyl 2-[[ethoxy
[(1-methylethyl) amino]phosphinothioy]oxy]benzoate, dimethyl
dichlorovinyl phosphate, O,O-diethyl S-ethyl-thiomethyl
phosphorodithioate, O,O-dimethyl S-(methyl-carbamoylmethyl)
phosphorodithioate, ethyl 3-methyl-4-(methylthio)phenyl
(1-methylethyl)-phosphoroamidate, O,O-dimethyl
O-[2-(methycarbanmoyl)-1-methyl-vinyl]phosphate, and
octamethylpyrophosphoramide.
Specific examples of phosphinates include: ethyl pentyl
phosphinate, ethyl hexyl phosphinate, ethyl heptyl phosphinate,
ethyl octyl phosphinate, ethyl decyl phosphinate, ethyl phenyl
phosphinate, butyl pentyl phosphinate, butyl hexyl phosphinate,
butyl heptyl phosphinate, pentyl dibutyl phosphinate, hexyl dibutyl
phosphinate, and heptyl dibutyl phosphinate.
Examples of phosphinic acids include: pentyl phosphinic acid, hexyl
phosphinic acid, heptyl phosphinic acid, octyl phosphinic acid,
decyl phosphinic acid, phenyl phosphinic acid, di pentyl phosphinic
acid, di heptyl phosphinic acid, di decyl phosphinic acid, di
phenyl phosphinic acid, phenyl hexyl phosphinic acid, and pentyl
decyl phosphinic acid.
Examples of phosphinous acids include: monopentyl phosphinous acid,
monohexyl phosphinous acid, monoheptyl phosphinous acid, monooctyl
phosphinous acid, monodecyl phosphinous acid, monophenyl
phosphinous acid, dipropyl phosphinous acid, dipentyl phosphinous
acid, diheptyl phosphinous acid, didecyl phosphinous acid, diphenyl
phosphinous acid, and propyl decyl phosphinous acid.
Examples of phosphonates include: hexyl pentyl phosphonate, heptyl
pentyl phosphonate, octyl pentyl phosphonate, decyl pentyl
phosphonate, phenyl pentyl phosphonate, dibutyl pentyl phosphonate,
dihexylphosphonate, heptylphosphonate, pentylphosphonate,
octylphosphonate, and phenylphosphonate.
Examples of phosphonic acids include: pentyl phosphonic acid, hexyl
phosphonic acid, heptyl phosphonic acid, octyl phosphonic acid,
decyl phosphonic acid, phenyl phosphonic acid, methyl pentyl
phosphonic acid, methyl phenyl phosphonic acid, pentylphosphonic
acid, octylphosphonic acid, phenylphosphonic acid, and pentyl
octylphosphonic acid.
Examples of phosphonites include: ethyl pentyl phosphonite, ethyl
hexyl phosphonite, ethyl heptyl phosphonite, ethyl octyl
phosphonite, ethyl decyl phosphonite, ethyl phenyl phosphonite,
butyl pentyl phosphonite, butyl hexyl phosphonite, butyl heptyl
phosphonite, diethyl pentyl phosphonite, diethyl hexyl phosphonite,
and diethyl heptyl phosphonite.
Examples of phosphonous acids include: 1-pentyl phosphonous acid,
2-pentyl phosphonous acid, 3-pentyl phosphonous acid, 1-hexyl
phosphonous acid, 2-hexyl phosphonous acid, 3-hexyl phosphonous
acid, 1-heptyl phosphonous acid, 2-heptyl phosphonous acid,
3-heptyl phosphonous acid, 4-heptyl phosphonous acid, octyl
phosphonous acid, decyl phosphonous acid, and phenyl phosphonous
acid.
The material of construction of the porous support of the composite
membrane is not critical to the invention. Any porous support that
provides physical strength to the discriminating layer may be
employed, so long as the pore sizes are sufficiently large to
permit the unhindered passage of permeate but not so large as to
interfere with the bridging-over of the resulting discriminating
layer. Typical pore sizes will range from 10 to 1,000 nanometers.
Typical support materials that are known in the art include
cellulose esters, polysulfones, polyether sulfones, polyvinyl
chloride, chlorinated polyvinyl chloride, polyvinylidene fluoride,
polystyrenes, polycarbonates, polyimides, polyacrylonitriles, and
polyesters. A particularly preferred class of support materials are
polysulfones. Preparation of such supports are described in U.S.
Pat. Nos. 3,926,798; 4,039,440; and 4,277,344, all of which are
incorporated herein by reference. The thickness of the microporous
support is usually 25 to 125 micrometers, and preferably from 40 to
75 micrometers.
A variety of membrane shapes are commercially available and useful
in the present invention. These include spiral wound, hollow fiber,
tubular, or flat sheet type membranes. In regard to the composition
of the membrane, often the discriminating layer has hygroscopic
polymers other than the polyamide coated upon the surface of the
discriminating layer. Among these polymers are anionic, cationic,
neutral and zwitterionic such as polymeric surfactants, polyvinyl
alcohol, polyethylene imine and polyacrylic acid.
The membranes of the present invention may be subjected to various
post treatments as described in U.S. Pat. Nos. 4,765,897; 5,876,602
and 5,755,964, all of which are incorporated herein by reference.
Such post treatments may further enhance membrane performance,
e.g., increased flux and/or decreased salt passage.
For example, as described in U.S. Pat. No. 5,876,602, membrane
stability to strong base exposure (while maintaining flux and salt
passage) can be achieved by contacting the membrane, after it has
been formed on a porous support, whether in flat sheet or element
form, with a hypochlorite solution at a pH of at least 10.5. The
optimal exposure time depends on the temperature and concentration
of the hypochlorite used. At room temperature, conditions which
achieve the stated goals can generally be found within the ranges
of 10 minutes to 5 hours and at concentrations of 200 to 10,000 ppm
by weight of hypochlorite, measured as chlorine. Preferred
concentrations of hypochlorite are 500 to 7,000 ppm; preferred
exposure times are 30 minutes to three hours. In a preferred
embodiment the membrane is subjected to a heat treatment before
being exposed to the aforementioned chlorine treatment. The
membranes are heated in water at a temperature of 40.degree. C. to
100.degree. C. for times of 30 seconds to 24 hours. The heat
treatment results in a further lowering of the salt passage and the
removal of impurities contained in the membrane which otherwise may
interfere in the beneficial results of the chlorine treatment.
Depending on the application desired, the two treatment conditions
can be adjusted within the ranges stated such that the salt passage
is improved while maintaining or even improving flux over either
treatment alone. The order in which the two treatments are
conducted is critical since heat treating the membrane
simultaneously with or subsequently to the chlorine treatment does
not provide the improved results obtained by first heat treating
the membrane followed by the chlorine treatment.
Another example of an applicable post treatment is described in
U.S. Pat. No. 5,755,964, which comprises contacting the
discriminating layer with an amine from the group consisting of:
ammonia optionally substituted with one or more alkyl groups of one
to two carbons which alkyl groups may be further optionally
substituted with one or more substituents selected from hydroxy,
phenyl, or amino; butylamine; cyclohexylamine; 1,6-hexanediamine
and mixtures thereof. Preferred substituted ammonia substances
include those such as dimethylamine; trimethylamine; ethylamine;
triethanolamine; N,N-dimethyl ethanolamine; ethylenediamine; and
benzylamine. It has been discovered that by contacting the above
amines with the discriminating layer, the flux is increased and the
rejection rates for particular substances may be changed. The
degree that the flux of the membrane is increased or enhanced may
be controlled by varying the particular amine employed, the
concentration of the amine, the time of contact between the
discriminating layer and amine, the temperature of the contact, the
pH of the amine solution, or combinations thereof. As the flux is
increased, the selectivity of the membrane may change, i.e., the
membrane may allow univalent ions such as sodium to pass through
the membrane at a higher rate while only rejecting divalent ions
and organic compounds.
The amine used to treat the polyamide discriminating layer may be
in solution, neat, or even a gas phase so long as it can be
contacted with the polyamide. Gas phases may typically be employed
for lower molecular weight amines such as ammonia, methylamine, and
dimethylamine. The solvent may be any solvent in which the amine is
soluble so long as the flux enhancement and the performance of the
membrane is not hindered by contact with the solvent. Typical
solvents may include water and organic compounds such as alcohols
and hydrocarbons provided the support is not dissolved by the
solvent. Generally, because of its ease of handling and its
availability, water is employed if a solvent is desired.
The extent that the flux of the membrane is enhanced when treated
with the amines of this invention varies depending upon the
particular amine employed. At least one general trend applies in
most situations, however. The trend being that the more functional
groups which are present on the amine, e.g., alcohol and/or amino
groups, the greater the increase in flux. Correspondingly, the
concentration of the amine and time of contact are interrelated and
affect the degree of flux enhancement. The minimum length of time
that a particular amine is required to be contacted with the
discriminating layer for an increase in flux depends to a great
extent upon the concentration of the amine. Generally, the higher
the concentration of the amine, the shorter the necessary length of
contacting time to increase the flux. In most cases, the
concentration of the amine should be at least about 5, preferably
at least about 20, most preferably at least about 50, to about 100
percent by weight. The minimum time of contact can be from at least
about 15 seconds, preferably at least about one minute, more
preferably at least about 30 minutes when contacted at ambient
temperatures.
In general, the longer the time of contact and the higher the
concentration of the amine, the greater the increase in flux. After
a prolonged time of contact, the flux will reach its maximum
increase and no longer increase. At this point, the membrane may be
used or continued to be stored in the amine. The time to reach the
maximum increase varies depending upon the particular amine
employed, the concentration of the amine, and the temperature of
contact but is ascertainable by one skilled in the art without
undue experimentation by utilizing the general trends disclosed
above. For most amines and concentrations, the flux of the membrane
will be maximized once the discriminating layer has been contacted
for about 5 days with the amine. If it is desired to shorten the
minimum length of time of contact, then the surface temperature of
the polyamide discriminating layer may be increased. Although this
applies generally, it is particularly advantageous if low
concentrations of an amine which might require a long contacting
time are being employed. Although temperature from about 0.degree.
to about 30.degree. C. are most conveniently used, increased
temperatures may shorten the necessary contacting time. The
increased temperatures should not be so high that the membrane's
performance is reduced, i.e., not above about 130.degree. C.
Typical temperatures which will hasten the flux effect of the
membrane are from at least about 30.degree. C., preferably at least
about 60.degree. C. to about 130.degree. C. These temperatures may
be reached by contacting the amine with the polyamide
discriminating layer in a device such as an oven or a dryer.
Typical ovens or dryers which may be employed include convection,
infrared, or forced air dryers.
The pH of the amine solution to be contacted with the polyamide is
not a critical aspect of the invention. However, the pH should not
be so low that the particular amine being employed precipitates out
of solution. On the other hand, the pH should not be so high that
the polyamide discriminating layer is degraded or performance is
negated. Preferably, a pH of about 7 to about 12 is useful in the
method of the present invention and for some amines higher pHs may
increase the degree of flux enhancement.
The method used to contact the amine with the discriminating layer
may be any which allows the amine to become associated with the
polyamide for a sufficient time to increase the flux. For instance,
the polyamide may be partially or totally immersed or soaked in the
amine or amine solution. The amine or amine solution may also be
passed through, sprayed onto, or rolled onto the discriminating
layer. Although the aforementioned methods may also be useful when
the amine is a gas, the contacting of a gaseous amine with the
discriminating layer is advantageously accomplished in a closed
vessel to minimize the amount of amine employed.
Improved flux and rejection properties can also be achieved by post
treating the subject membranes by contacting the membranes with a
strong mineral acid, e.g. phosphoric acid, polyphosphoric acid,
phosphorous acid, sulfuric acid, etc. Phosphoric acid at
concentrations of from about 10 to about 85 weight percent are
particularly preferred. As described in U.S. Pat. No. 4,765,987,
the membrane may be contacted with the mineral acid, e.g., by
spraying an aqueous acid solution onto the membrane, dipping the
membrane in an aqueous acid bath, etc. In some embodiments the acid
solution may be heated. Once treated with the mineral acid, the
membrane may be further treated with the rejection enhancing
agents, e.g., colloids, tannic acid, polyamidoamines, etc, as
described in U.S. Pat. No. 4,765,897.
As used herein the following terms have the definitions provided:
"rejection rate" is the percentage of a particular dissolved or
dispersed material (i.e., solute) which does not flow through the
membrane with the solvent. The rejection rate is equal to 100 minus
the percentage of dissolved or dispersed material which passes
through the membrane, i.e., solute passage, "salt passage" if the
dissolved material is a salt. "Flux" is the flow rate per unit area
at which solvent, typically water, passes through the membrane.
"Reverse osmosis membrane" is a membrane which has a rejection rate
for NaCl of from about 95 to about 100 percent. "Nanofiltration
membrane" is a membrane which has a rejection rate for NaCl of from
about 0 to about 95 percent and has a rejection rate for at least
one divalent ion or organic compound of from about 20 to about 100
percent. "Polyamide" is a polymer in which amide linkages
(--C(O)NH--) occur along the molecular chain. "Complexing agent",
"amine" and "acyl halide" are intended to mean a single species or
multiple species of compounds intermixed. For example, the term
"amine" may make reference to a mixture of polyfunctional amine
monomers. The terms "percent by weight", "percent weight" and
"weight percent" are intended to mean 100.times.(gram of solute/100
milliliters of solvent).
EXAMPLES
The following examples are intended to help illustrate the
invention and should not be construed to limit the scope of the
appended claims. Except where indicated otherwise, composite
membranes were made in the laboratory using a porous polysulfone
support formed from a 16.5 percent polysulfone solution in DMF. The
support was cut into rectangles (11 in. by 7 in.), clipped onto
wire frames (10 in. by 7.5 in.) and placed in a 2.5 weight percent
meta phenylene diamine (MPD) solution for approximately 20 minutes.
The MPD soaked supports were then placed on a paper towel and
rolled with a rubber roller to remove excess solution from both the
back and front sides. The support was then placed on a plastic
sheet and a silicone rubber gasket placed around the edge. A
plastic sheet was cut with the opening being the same size as the
opening in the gasket. This was clamped to form a leak proof seal
at the edge. 50 ml of a Isopar L solution of trimesyol chloride
(TMC) (0.09 weight percent) containing a 1:2 stoichiometric ratio
(TMC: complexing agent) of the complexing agent of interest was
then poured on top. The specific complexing agent utilized in each
example is provided in the Tables below. Control samples contained
no complexing agent. After 1 minute of reaction, the TMC solution
was poured off and the membrane was rinsed with hexane and allowed
to dry for the period of time specified in the Tables below. The
formed composite membrane was then placed in water and tested using
a 2000 ppm NaCl solution with a pH between 6.5 and 8 at 130 psi
applied pressure. The membranes were run under these test
conditions for 30 min and then the permeate was collected and
analyzed. The results are provided in the Tables below. Due to the
variability in preparation and testing conditions, a separate
control membrane was prepared and tested with each prepared batch
of membranes, as indicated in each Table below.
TABLE 1 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 1 (control) none 60 11.7 0.79 2 Tri-methyl
phosphate 60 23.3 2.7 3 Tri-ethyl phosphate 60 13.4 0.46 4
Tri-butyl phosphate 60 20.3 0.88
TABLE 2 Dry Time Salt Passage Example No. Complexing Agent (sec)
Flux (gfd) (%) 5 (control) none 60 12.1 1.2 6 Dibutyl phosphite 60
14.4 0.62
TABLE 3 Dry Time Salt Passage Example No. Complexing Agent (sec)
Flux (gfd) (%) 7 (control) none 10 14.7 0.7 8 Bis(2-ethyl hexyl) 10
23.7 1.06 phosphite
TABLE 4 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 9 (control) none 10 13.7 0.69 10 Tri phenyl
phosphine 10 22.11 2.6 11 Triethyl phosphate 10 20.5 1.5
TABLE 5 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 12 (control) none 10 16.6 0.26 13 Tri phenyl
phosphine 10 31.8 3.32 14 Tri phenyl phosphate 10 22.9 0.34
TABLE 6 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 15 (control) none 10 12.6 0.35 16 Tri phenyl
phosphine 10 17.7 0.41 17 Tri butyl phosphate 10 16.2 0.53
TABLE 7 Salt Dry Time Flux Passage Example No. Complexing Agent
(sec) (gfd) (%) 18 (control) none 10 12.0 0.38 19 Ditertbutyl
diisopropyl 10 16.0 0.45 Phosphoramidite [(CH.sub.3).sub.2
CH].sub.2 NP[OC(CH.sub.3).sub.3 ].sub.2
TABLE 8 Salt Passage Example Dry Time Flux (per- No. Complexing
Agent (seconds) (gfd) cent) 20 none 10 13.8 0.38 (control) 21
Dibutylbutyl Phosphonate 10 16.1 0.30 CH.sub.3 (CH.sub.2).sub.3
P(O)[O(CH.sub.2).sub.3 CH.sub.3 ].sub.2 22 *Tri-octyl phosphine 10
17.5 0.39 *4:1 stoichiometric ratio of TMC to Tri-octyl
phosphine
TABLE 9 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 23 (control) none 30 11.9 0.49 24 50 mM Ferrocene
30 14.7 0.39 25 100 mM Ferrocene 30 16.5 0.37
TABLE 10 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 26 (control) none 10 14.2 0.341 27 5 mM Triphenyl
Bismuth 10 12.8 0.341
TABLE 11 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 28 (Control) none 10 16.6 0.259 29 2.5 mM Triphenyl
Phosphine 10 31.8 3.32 30 2.5 mM Triphenyl Phosphate 10 22.9 0.343
31 2.5 mM Triphenyl Arsine 10 29.9 0.498 32 2.5 mM Triphenyl
Antimony 10 25.1 0.442
Tables 10 and 11 highlight differences in preformance associated
with various triphenyl metal and nonmetal complexing agents. As
shown in Table 10, when used in a system comprising TMC and Isopar
L solvent, trioctyl bismuth is not a preferred complexing
agent.
TABLE 12 Dry Time Flux Salt Passage Example No. Complexing Agent
(sec) (gfd) (%) 33 (Control) None 10 13.7 0.30 34 3 mM, Trioctyl
Aluminum 10 40.9 72 35 5 mM, Tributyl Phosphate 10 19.47 0.42
Table 12 highlights the difference in performance between a
preferred complexing agent for use with TMC and Isopar L solvent
(ex. 35) and a complexing agent (ex. 34) which is believed to
possess a total energy value above the desired range for the
subject invention as evidenced by an unexcepable salt passage.
TABLE 13 Drying Salt Passage Example No. Complexing Agent Time
(sec) Flux (gfd) (%) 36 (Control) none 10 19.0 0.45 37 Fe (III)
Tris TMH 10 16.72 0.326 38 Fe (II) Bis Acac 10 22.8 0.65 39 Fe
(III) Tris Acac 10 24.0 0.71
TABLE 14 Dry Salt Passage Example No. Complexing Agent Time (sec)
Flux (gfd) (%) 40 (Control) none 10 18.3 0.48 41 Co(III) Tris Acac
10 19.5 0.96 42 Cr(III) Tris Acac 10 22.0 0.50
The term "Acac" represents Acetylacetonate (2,4 pentane-dione) and
"TMH" represents 2,2,6,6 tetramethyl-3,5 heptanedionate. Testing
for examples 36-42 was completed at 150 psi and 2000 ppm NaCl. The
TMC solution for example 37 was made at a concentration of 2.5 mM
of complexing agent; whereas, the TMC solutions for examples 38,
39, 41 and 42 were saturated solutions not containing the remaining
undissolved portion. Therefore the solutions used in examples 38,
39, 41, and 42 are of less concentration that 2.5 mM.
As shown in the Tables provided above, the addition of the subject
complexing agents to the polyfunctional acyl halide solution can
improve flux and/or rejection (e.g., salt passage) of the resulting
membranes.
* * * * *